JP5907424B2 - Sterilizer - Google Patents

Sterilizer Download PDF

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JP5907424B2
JP5907424B2 JP2012086816A JP2012086816A JP5907424B2 JP 5907424 B2 JP5907424 B2 JP 5907424B2 JP 2012086816 A JP2012086816 A JP 2012086816A JP 2012086816 A JP2012086816 A JP 2012086816A JP 5907424 B2 JP5907424 B2 JP 5907424B2
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heat exchanger
steam
valve
water
cooling
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JP2013215111A (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や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。特に、処理槽と熱交換器との間で水を循環させ、その循環水を熱交換器において蒸気により加熱するか冷却水により冷却するかを切り替える殺菌装置に関するものである。   The present invention relates to a sterilization apparatus used for heat sterilization of a retort food or the like and subsequent cooling. In particular, the present invention relates to a sterilizer that circulates water between a treatment tank and a heat exchanger and switches between circulating water being heated by steam or cooling by cooling water in the heat exchanger.

従来、下記特許文献1に開示されるように、処理槽(1)内に被処理物(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)からの冷却水で冷却するかを切り替えて、被処理物(2)の加熱殺菌とその後の冷却を図ることのできる殺菌装置が知られている。   Conventionally, as disclosed in Patent Document 1 below, the processing object (2) is accommodated in the processing tank (1) and water is stored, and the stored water is circulated between the heat exchanger (3). The circulating water is heated with steam in the heat exchanger (3) or cooled with cooling water from the cooling tower (8) to switch the sterilization of the workpiece (2) and subsequent cooling. Sterilizers that can do this are known.

特許第4229420号公報Japanese Patent No. 4229420

この種の殺菌装置では、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が供給され、その後の冷却工程では熱交換器に冷却水が供給される。そのため、殺菌工程から冷却工程への移行直後、蒸気が充満した熱交換器内には冷却水がいきなり導入されることになり、ウォーターハンマが発生し、熱交換器への配管から音や衝撃が発生したり、配管内の残留蒸気が安全弁から噴き出したりする不都合があった。   In this type of sterilizer, steam is supplied to the heat exchanger in the sterilization step while circulating water between the treatment tank and the heat exchanger, and cooling water is supplied to the heat exchanger in the subsequent cooling step. . Therefore, immediately after the transition from the sterilization process to the cooling process, cooling water is suddenly introduced into the heat exchanger filled with steam, water hammer is generated, and noise and impact are generated from the piping to the heat exchanger. There are inconveniences that occur or residual steam in the piping is ejected from the safety valve.

そこで、本発明が解決しようとする課題は、殺菌工程後の冷却工程において、ウォーターハンマの発生を防止して、熱交換器への配管からの音や衝撃を解消または軽減し、また、安全弁からの蒸気の噴き出しを防止することにある。   Therefore, the problem to be solved by the present invention is to prevent the occurrence of water hammer in the cooling process after the sterilization process, to eliminate or reduce the noise and impact from the piping to the heat exchanger, and from the safety valve. It is to prevent the jet of steam.

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、この貯留水を前記処理槽と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中、前記熱交換器に供給された蒸気の凝縮水をスチームトラップを介して外部へ排出するドレン排出手段と、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、前記熱交換器からの蒸気排出を図る排蒸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 in order to solve the above-mentioned problems. The invention according to claim 1 is a treatment tank in which water is stored while an object to be treated is stored, and the stored water is treated as 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 steam supplied to the heat exchanger during the steam supply to the heat exchanger by the steam supplying means to the outside through a steam trap Drain discharge means for discharging, and steam discharge from the heat exchanger after the steam supply to the heat exchanger by the steam supply means is stopped and before the cooling water supply to the heat exchanger is started by the cooling means. It is characterized by having a steaming means for achieving A filtering apparatus.

請求項1に記載の発明によれば、給蒸手段による熱交換器への蒸気供給の停止後、冷却手段による熱交換器への冷却水供給の開始前に、排蒸手段により熱交換器からの蒸気排出を図ることができる。従って、その後、冷却手段により熱交換器に冷却水を供給しても、ウォーターハンマの発生を防止して、熱交換器への配管からの音や衝撃を解消または軽減することができる。また、安全弁からの蒸気の噴き出しを防止することができる。   According to the first aspect of the present invention, after the steam supply to the heat exchanger by the steam supply means is stopped, before the cooling water supply to the heat exchanger by the cooling means is started, the steam exhausting means removes the heat exchanger from the heat exchanger. The steam can be discharged. Therefore, even if cooling water is supplied to the heat exchanger by the cooling means thereafter, the generation of a water hammer can be prevented, and the noise and impact from the piping to the heat exchanger can be eliminated or reduced. Further, it is possible to prevent the vapor from being ejected from the safety valve.

請求項2に記載の発明は、前記給蒸手段は、前記熱交換器への給蒸路に給蒸弁を備え、前記排蒸手段は、前記熱交換器からの排蒸路に排蒸弁を備え、前記冷却手段は、前記熱交換器への冷却水送り路に冷却水送り弁を備え、前記排蒸路は、前記給蒸弁よりも下流の前記給蒸路に接続される管路、または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管路を備え、この管路に前記排蒸弁が設けられてい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 steam supply means includes a steam supply valve in a steam supply path to the heat exchanger, and the steam exhaust means has a steam exhaust valve in a steam supply path from the heat exchanger. The cooling means includes a cooling water feed valve in the cooling water feed path to the heat exchanger, and the exhaust steam path is a pipe line connected to the steam feed path downstream from the steam feed valve. Or a pipe line connected to the cooling water feed path downstream from the cooling water feed valve, wherein the exhaust steam valve is provided in the pipe line. Device.

請求項2に記載の発明によれば、熱交換器への給蒸、熱交換器からの排蒸、熱交換器への冷却水の通水を、それぞれ弁の開閉で制御することができる。また、給蒸路や冷却水送り路に接続した管路に排蒸弁を設けることで、熱交換器やそれへの配管からの蒸気排出を円滑に行うことができる。   According to the second aspect of the present invention, the steam supply to the heat exchanger, the exhaust from the heat exchanger, and the flow of the cooling water to the heat exchanger can be controlled by opening and closing the valves, respectively. In addition, by providing the exhaust steam valve in the pipe connected to the steam supply path or the cooling water feed path, the steam can be smoothly discharged from the heat exchanger and the piping to it.

さらに、請求項3に記載の発明は、前記排蒸弁と前記冷却水送り弁とを閉じる一方、前記給蒸弁を開けて、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、前記給蒸弁を閉じる一方、前記排蒸弁を開け、前記排蒸弁を開けてから排蒸時間経過すると、前記排蒸弁を閉じ、前記冷却水送り弁を開けて、前記冷却手段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することを特徴とする請求項2に記載の殺菌装置である。   Furthermore, the invention according to claim 3 closes the exhaust steam valve and the cooling water feed valve, and opens the steam supply valve to supply steam from the steam supply means to the heat exchanger. By heating the circulating water, the object to be treated is sterilized, and when the inside of the treatment tank is at a sterilization temperature or higher and the sterilization time has elapsed, the steam supply valve is closed while the steaming valve is opened. When the evacuation time has elapsed since opening, the evacuation valve is closed, the cooling water feed valve is opened, the cooling water from the cooling means is supplied to the heat exchanger, and the circulating water is cooled. The sterilization apparatus according to claim 2, wherein the object to be treated is cooled.

請求項3に記載の発明によれば、被処理物の殺菌工程、熱交換器やそれへの配管からの排蒸工程、および被処理物の冷却工程を順次に実行し、排蒸工程後に冷却工程を実行することで、冷却工程においてウォーターハンマを生じさせるおそれがない。   According to the third aspect of the present invention, the sterilization process of the object to be processed, the steaming process from the heat exchanger and the piping to the heat exchanger, and the cooling process of the object to be processed are sequentially performed, and cooling is performed after the steaming process. By executing the process, there is no possibility of causing a water hammer in the cooling process.

本発明によれば、殺菌工程後の冷却工程において、ウォーターハンマの発生を防止して、熱交換器への配管からの音や衝撃を解消または軽減することができる。また、安全弁からの蒸気の噴き出しを防止することができる。   ADVANTAGE OF THE INVENTION According to this invention, generation | occurrence | production of a water hammer can be prevented in the cooling process after a sterilization process, and the sound and impact from piping to a heat exchanger can be eliminated or reduced. Further, it is possible to prevent the vapor from being ejected from the safety valve.

本発明の殺菌装置の一実施例を示す概略図である。It is the schematic which shows one Example of the sterilizer of this invention.

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 retort 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内からの排水手段5と、処理槽3内の加圧手段6と、処理槽3内からの排気手段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やそれへの配管内から蒸気を排出する排蒸手段13と、これら各手段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 from the treatment tank 3, and a treatment tank 3. Pressurizing means 6, exhaust means 7 from inside 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 steam discharge means 13 for discharging the steam from the heat exchanger 8 and the piping to the heat exchanger 8, and a control means (not shown) for controlling these means.

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。従って、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。   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. Therefore, the workpiece 2 can be taken in and out of the processing tank 3 by opening the door, and the opening of the processing tank 3 can be airtightly closed by closing the door.

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)が設けられている。   The treatment tank 3 is provided with a temperature sensor 14 for detecting the temperature in the treatment tank 3 and a water level detector (not shown) for detecting the water level in the treatment tank 3.

なお、図示例の場合、被処理物2は、トレー15に並べられ、そのようなトレー15が上下に積み重ねられて処理槽3内に収容されている。トレー15は、上方へ開口した浅い矩形状の容器であり、少なくとも底面に多数の開口が形成されると共に、上下のトレー15,15は、側面において隙間をあけて積み重ねられる。但し、被処理物2は、処理槽3の棚に載せたり、ワゴンに載せたりして、処理槽3内に収容されてもよい。   In the case of the illustrated example, the objects to be processed 2 are arranged in a tray 15, and such trays 15 are stacked in the vertical direction and accommodated in the processing tank 3. The tray 15 is a shallow rectangular container that opens upward. At least a plurality of openings are formed on the bottom surface, and the upper and lower trays 15 and 15 are stacked with gaps on the side surfaces. However, the workpiece 2 may be accommodated in the processing tank 3 by placing it on a shelf of the processing tank 3 or by placing it on a wagon.

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が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 the to-be-processed object 2 accommodated in the processing tank 3 does not immerse.

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内へ加圧空気(言い換えれば圧縮空気)を供給する。加圧路21に設けた加圧弁22を開くことで、加圧空気源からの加圧空気を処理槽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 pressurized air (in other words, compressed air) into the processing tank 3 through the pressurizing passage 21. By opening the pressurizing valve 22 provided in the pressurizing passage 21, pressurized air from a pressurized air source can be supplied into the processing tank 3, and the inside of the processing tank 3 can be pressurized to a pressure exceeding the 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、処理槽3の側から順に、排気弁24と逆止弁25とが設けられている。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 an exhaust valve 24 and a check valve 25 are provided in order from the processing tank 3 side. 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。なお、熱交換器8は、その構成を特に問わないが、本実施例ではプレート式熱交換器とされている。   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. In addition, although the structure in particular is not ask | required for the heat exchanger 8, it is set as the plate type heat exchanger in a present Example.

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26と循環ポンプ27とを備える。循環路26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26は、循環ポンプ27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28に接続されている。このノズル28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27からの水を被処理物2へ向けて噴射する。なお、図示例の場合、給水路16と循環路26とは、処理槽3の底部の側で共通の管路とされている。   The circulation means 9 circulates water between the treatment tank 3 and the heat exchanger 8. The circulation means 9 includes a circulation path 26 and a circulation pump 27. One end of the circulation path 26 is connected to the bottom of the treatment tank 3, and the circulation path 26 from the bottom of the treatment tank 3 passes through the circulation pump 27 and the heat exchanger 8 in this order, and the other end is the treatment tank 3. It is connected to the inner nozzle 28. This nozzle 28 is provided in the side part and / or upper part in the processing tank 3, and injects the water from the circulation pump 27 toward the to-be-processed object 2. FIG. In the case of the illustrated example, the water supply path 16 and the circulation path 26 are a common pipe line on the bottom side of the treatment tank 3.

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29を備え、この給蒸路29には遮断弁30と給蒸弁31とが設けられている。給蒸手段10による熱交換器8への蒸気供給時、遮断弁30は開放状態に維持され、給蒸弁31の開度が調整される。給蒸弁31の開度を調整することで、循環手段9による循環水の温度、ひいては処理槽3内の温度を、所望に調整することができる。具体的には、温度センサ14の検出温度に基づき、給蒸弁31の開度が調整される。   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 29 that supplies steam from the boiler to the heat exchanger 8, and a shutoff valve 30 and a steam supply valve 31 are provided in the steam supply path 29. When supplying steam to the heat exchanger 8 by the steam supply means 10, the shutoff valve 30 is maintained in an open state, and the opening degree of the steam supply valve 31 is adjusted. By adjusting the opening degree of the steam supply valve 31, the temperature of the circulating water by the circulation means 9 and thus the temperature in the treatment tank 3 can be adjusted as desired. Specifically, the opening degree of the steam supply valve 31 is adjusted 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32を備え、クーリングタワー32にて冷却された水は、送水ポンプ33により、冷却水送り路34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35を介してクーリングタワー32へ戻される。図示例の場合、冷却水送り路34と給蒸路29とは、熱交換器8の側で共通の管路とされている。なお、クーリングタワー32には、ボールタップ36を介して適宜給水される。   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 32, and water cooled by the cooling tower 32 is supplied to the heat exchanger 8 by the water pump 33 via the cooling water feed path 34, and the water after passing through the heat exchanger 8. Is returned to the cooling tower 32 via the cooling water return path 35. In the case of the illustrated example, the cooling water feed path 34 and the steam supply path 29 are common pipe lines on the heat exchanger 8 side. The cooling tower 32 is appropriately supplied with water via a ball tap 36.

冷却水送り路34には冷却水送り弁37が設けられる一方、冷却水戻し路35には冷却水戻し弁38が設けられている。冷却水送り路34と給蒸路29との合流部は、冷却水送り弁37や給蒸弁31より下流側(熱交換器8側)に配置されている。また、冷却水送り弁37より上流側(クーリングタワー32側)の冷却水送り路34と、冷却水戻し弁38より下流側(クーリングタワー32側)の冷却水戻し路35とは、バイパス路39で接続されており、このバイパス路39にはバイパス弁40が設けられている。   A cooling water feed valve 37 is provided in the cooling water feed path 34, while a cooling water return valve 38 is provided in the cooling water return path 35. The junction between the cooling water feed path 34 and the steam supply path 29 is disposed downstream of the cooling water feed valve 37 and the steam supply valve 31 (on the heat exchanger 8 side). Further, a cooling water feed path 34 on the upstream side (cooling tower 32 side) from the cooling water feed valve 37 and a cooling water return path 35 on the downstream side (cooling tower 32 side) from the cooling water return valve 38 are connected by a bypass path 39. A bypass valve 40 is provided in the bypass passage 39.

従って、バイパス弁40を閉じる一方、冷却水送り弁37および冷却水戻し弁38を開いた状態で、送水ポンプ33を作動させると、クーリングタワー32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37および冷却水戻し弁38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。この際、送水ポンプ33を停止させてもよいが、クーリングタワー32の凍結防止のために、バイパス弁40を開いた状態で送水ポンプ33を作動させてもよい。   Accordingly, when the water feed pump 33 is operated with the bypass valve 40 closed and the coolant feed valve 37 and the coolant return valve 38 opened, the coolant is circulated between the cooling tower 32 and the heat exchanger 8. be able to. On the other hand, if the cooling water feed valve 37 and the cooling water return valve 38 are closed, the flow of the cooling water to the heat exchanger 8 can be stopped. At this time, the water pump 33 may be stopped, but the water pump 33 may be operated with the bypass valve 40 opened in order to prevent the cooling tower 32 from freezing.

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35の内、冷却水戻し弁38より上流側(熱交換器8側)に設けられ、冷却水戻し路35から分岐するドレン排出路41に、ドレン排出弁42、スチームトラップ43および逆止弁44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42を開けておくことで、蒸気の凝縮水を下方へ脱落させて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 on the upstream side (heat exchanger 8 side) of the cooling water return valve 38 in the cooling water return path 35, and is connected to the drain discharge path 41 branched from the cooling water return path 35. 42, a steam trap 43 and a check valve 44 are provided in this order. When the steam is supplied to the heat exchanger 8, by opening the drain discharge valve 42, the condensed water of the steam can be dropped downward and discharged to the outside.

排蒸手段13は、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、熱交換器8や配管内に残った蒸気を外部へ排出する。排蒸手段13は、熱交換器8の側からの排蒸路45を備え、この排蒸路45には排蒸弁46と逆止弁47とが設けられている。排蒸路45は、給蒸弁31よりも下流の給蒸路29に接続される管路、または冷却水送り弁37よりも下流の冷却水送り路34に接続される管路を備える。言い換えれば、排蒸路45は、給蒸弁31よりも下流の給蒸路29、または冷却水送り弁37よりも下流の冷却水送り路34から分岐するように設けられる。本実施例では、給蒸路29の内、給蒸弁31よりも下流で、且つ冷却水送り路34との合流部よりも上流に、排蒸路45が分岐するように設けられている。また、排蒸路45には、給蒸路29との分岐部と排蒸弁46との間に、安全弁48が設けられている。   After the steam supply to the heat exchanger 8 is stopped by the steam supply means 10, the exhaust steam means 13 remains in the heat exchanger 8 or the piping before the cooling means 11 starts supplying the cooling water to the heat exchanger 8. The steam is discharged to the outside. The steaming means 13 includes a steaming path 45 from the heat exchanger 8 side, and a steaming valve 46 and a check valve 47 are provided in the steaming path 45. The exhaust steam path 45 includes a pipe line connected to the steam feed path 29 downstream of the steam feed valve 31 or a pipe line connected to the cooling water feed path 34 downstream of the cooling water feed valve 37. In other words, the exhaust steam passage 45 is provided so as to branch from the steam supply passage 29 downstream of the steam supply valve 31 or the cooling water feed passage 34 downstream of the cooling water feed valve 37. In the present embodiment, in the steam supply passage 29, the exhaust steam passage 45 is provided so as to branch downstream from the steam supply valve 31 and upstream from the junction with the cooling water feed passage 34. Further, a safety valve 48 is provided in the exhaust steam path 45 between the branching section with the steam supply path 29 and the exhaust steam valve 46.

制御手段は、温度センサ14や水位検出器の検出信号や経過時間などに基づき、前記各手段を制御する制御器(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27、遮断弁30、給蒸弁31、クーリングタワー32、送水ポンプ33、冷却水送り弁37、冷却水戻し弁38、バイパス弁40、ドレン排出弁42、排蒸弁46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。   The control means is a controller (not shown) that controls each means based on the detection signal of the temperature sensor 14 and the water level detector, the elapsed time, and the like. 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 27, the shutoff valve 30, the steam supply valve 31, the cooling tower 32, the water supply pump 33, and the cooling water supply valve 37. In addition to the cooling water return valve 38, the bypass valve 40, the drain discharge valve 42, and the steam exhaust valve 46, the temperature sensor 14 and the water level detector are connected to the controller.

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、排蒸工程、冷却工程および排水工程を順次に実行する。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および排蒸弁46は開かれ、その他の弁は閉じられており、各ポンプは停止している。   As will be described below, the controller performs heat sterilization of the workpiece 2 in the processing tank 3 and subsequent cooling in accordance with a predetermined procedure (program). Typically, a water supply process, a transition process, a sterilization process, a steaming process, a cooling process, and a draining process are sequentially performed. 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 and the exhaust valve 46 are opened, the other valves are closed, and the respective pumps 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。この際、排水弁20および加圧弁22は閉じられており、排気弁24は開かれている。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 step In the water supply step, 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. At this time, the drain valve 20 and the pressurizing valve 22 are closed, and the exhaust valve 24 is opened. 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27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28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、給蒸弁31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。この際、冷却水送り弁37、冷却水戻し弁38および排蒸弁46は閉じられており、ドレン排出弁42は開かれている。ドレン排出弁42を開いておくことで、蒸気の凝縮水は、スチームトラップ43を介して排出される。
(2) Transition process In the transition process, 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 and processed. The temperature in the tank 3 is raised to the sterilization temperature. Specifically, by operating the circulation pump 27, the water from the inner bottom of the processing tank 3 is returned to the processing tank 3 from the nozzle 28 via the heat exchanger 8, thereby exchanging heat with the processing tank 3. Water is circulated to and from the vessel 8. Further, the steam supply valve 31 is 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. At this time, the cooling water feed valve 37, the cooling water return valve 38, and the exhaust steam valve 46 are closed, and the drain discharge valve 42 is opened. By opening the drain discharge valve 42, the steam condensate is discharged through the steam trap 43.

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包装(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やや高圧)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 packaging (a 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 (slightly 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による水の循環と、処理槽3内の加圧とは、冷却工程の終了まで引き続きなされる。つまり、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、殺菌温度相当の飽和蒸気圧力よりもやや高圧に、冷却工程の終了まで維持される。   Thereafter, the water circulation by the circulation means 9 and the pressurization in the treatment tank 3 are continued until the end of the cooling step. That is, 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 to a slightly higher pressure than the saturated vapor pressure corresponding to the sterilization temperature after the inside of the treatment tank 3 rises to the sterilization temperature until the end of the cooling process. .

(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と熱交換器8との間で水を循環させつつ、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31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31およびドレン排出弁42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 a sterilization process, the temperature in the processing tank 3 is hold | maintained at the sterilization temperature, and the to-be-processed object 2 is heated and sterilized. Specifically, the opening degree of the steam supply valve 31 is adjusted so that the temperature detected by the temperature sensor 14 is maintained at the sterilization temperature while water is circulated between the treatment tank 3 and the heat exchanger 8. 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 31 and the drain discharge valve 42 are closed, the steam supply to the heat exchanger 8 is stopped, and the sterilization process is terminated.

(4)排蒸工程
排蒸工程では、排蒸手段13により、熱交換器8やそれに接続された配管内から残留蒸気を外部へ排出する。具体的には、排蒸弁46を開けることで、熱交換器8や配管内の圧力を開放し、熱交換器8内やそれへの給蒸路29(給蒸弁31と熱交換器8との間の給蒸路29)や冷却水送り路34(冷却水送り弁37と熱交換器8との間の冷却水送り路34)内に残留する蒸気を外部へ排出する。排蒸弁46の開放から所定の排蒸時間を経過すると、排蒸弁46を閉じて、排蒸工程を終了する。
(4) Steaming process In the steaming process, the steam is discharged from the heat exchanger 8 and the pipe connected thereto by the steaming means 13 to the outside. Specifically, by opening the steam exhaust valve 46, the pressure in the heat exchanger 8 and the piping is released, and the steam supply path 29 (the steam supply valve 31 and the heat exchanger 8) to the heat exchanger 8 and to the heat exchanger 8 is released. The steam remaining in the steam supply path 29) and the cooling water feed path 34 (the cooling water feed path 34 between the cooling water feed valve 37 and the heat exchanger 8) is discharged to the outside. When a predetermined steaming time elapses from the opening of the steaming valve 46, the steaming valve 46 is closed and the steaming process is terminated.

(5)冷却工程
冷却工程では、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において冷却手段により冷却して、これにより処理槽3内の被処理物2の冷却を図る。具体的には、冷却水送り弁37および冷却水戻し弁38を開いた状態で、クーリングタワー32および送水ポンプ33を作動させて、熱交換器8に冷却水を循環させればよい。この際、給蒸弁31、ドレン排出弁42、排蒸弁46およびバイパス弁40は閉じられている。
(5) Cooling step In the cooling step, while circulating water between the treatment tank 3 and the heat exchanger 8, the circulating water is cooled by the cooling means in the heat exchanger 8, thereby The workpiece 2 is cooled. Specifically, the cooling water may be circulated through the heat exchanger 8 by operating the cooling tower 32 and the water pump 33 with the cooling water feed valve 37 and the cooling water return valve 38 opened. At this time, the steam supply valve 31, the drain discharge valve 42, the steam discharge valve 46, and the bypass valve 40 are closed.

冷却工程の開始から設定時間経過するか、処理槽3内の温度(冷却水の温度)が設定温度よりも下がってから設定時間経過すると、冷却水送り弁37および冷却水戻し弁38を閉じて、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。   When the set time elapses from the start of the cooling process or when the set time elapses after the temperature in the treatment tank 3 (cooling water temperature) falls below the set temperature, the cooling water feed valve 37 and the cooling water return valve 38 are closed. The cooling process is finished. 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.

(6)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。
(6) 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.

本実施例の殺菌装置1によれば、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、排蒸手段13により熱交換器8や配管(29,34)内の蒸気を排出して圧力が開放される。従って、その後、冷却手段11により熱交換器8に冷却水を供給しても、ウォーターハンマの発生を防止して、熱交換器8への配管からの音や衝撃を解消または軽減することができる。また、安全弁48からの蒸気の噴き出しを防止することもできる。   According to the sterilization apparatus 1 of the present embodiment, 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 starts, the steaming means 13. As a result, the steam in the heat exchanger 8 and the pipes (29, 34) is discharged and the pressure is released. Therefore, even if the cooling water is supplied to the heat exchanger 8 by the cooling means 11 thereafter, the generation of water hammer can be prevented, and the noise and impact from the piping to the heat exchanger 8 can be eliminated or reduced. . Further, it is possible to prevent the vapor from being ejected from the safety valve 48.

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を備えた殺菌装置1において、熱交換器8への蒸気供給の停止後、熱交換器8への冷却水供給の開始前に、熱交換器8からの蒸気排出を図る構成であれば、排蒸手段13の設置位置など、その他の構成および制御は適宜に変更可能である。   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, in the sterilization apparatus 1 including the heat exchanger 8, the steam is discharged from the heat exchanger 8 after the supply of steam to the heat exchanger 8 is stopped and before the cooling water supply to the heat exchanger 8 is started. If it is a structure, other structures and controls, such as the installation position of the dehumidification means 13, can be changed suitably.

さらに、加圧手段6は、前記実施例では加圧空気を用いたが、場合により不活性ガスを用いてもよい。   Further, although the pressurizing means 6 uses pressurized air in the above embodiment, an inert gas may be used in some cases.

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 排蒸手段
29 給蒸路
31 給蒸弁
45 排蒸路
46 排蒸弁
34 冷却水送り路
35 冷却水戻し路
37 冷却水送り弁
38 冷却水戻し弁
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 Steaming means 11 Cooling means 12 Drain discharge means 13 Dehumidification means 29 Steam supply path 31 Steam supply valve 45 Waste steam path 46 Waste steam valve 34 Cooling water feed path 35 Cooling water return path 37 Cooling water feed valve 38 Cooling water return 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、
この貯留水を前記処理槽と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中、前記熱交換器に供給された蒸気の凝縮水をスチームトラップを介して外部へ排出するドレン排出手段と、
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、前記熱交換器からの蒸気排出を図る排蒸手段と
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;
A circulating means for circulating the stored water between the treatment tank and 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;
During steam supply to the heat exchanger by the steam supply means, drain discharge means for discharging the condensed water of the steam supplied to the heat exchanger to the outside through a steam trap;
After the steam supply to the heat exchanger by the steam supply means is stopped, and before the cooling water supply to the heat exchanger is started by the cooling means, steam exhaust means for discharging steam from the heat exchanger; A sterilizer characterized by comprising.
前記給蒸手段は、前記熱交換器への給蒸路に給蒸弁を備え、
前記排蒸手段は、前記熱交換器からの排蒸路に排蒸弁を備え、
前記冷却手段は、前記熱交換器への冷却水送り路に冷却水送り弁を備え、
前記排蒸路は、前記給蒸弁よりも下流の前記給蒸路に接続される管路、または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管路を備え、この管路に前記排蒸弁が設けられている
ことを特徴とする請求項1に記載の殺菌装置。
The steam supply means includes a steam supply valve in a steam supply path to the heat exchanger,
The steaming means includes a steaming valve in a steaming path from the heat exchanger,
The cooling means includes a cooling water feed valve in a cooling water feed path to the heat exchanger,
The exhaust steam path includes a pipe line connected to the steam feed path downstream from the steam feed valve, or a pipe line connected to the cooling water feed path downstream from the cooling water feed valve. The sterilizer according to claim 1, wherein the steaming valve is provided in a pipe line.
前記排蒸弁と前記冷却水送り弁とを閉じる一方、前記給蒸弁を開けて、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、前記給蒸弁を閉じる一方、前記排蒸弁を開け、
前記排蒸弁を開けてから排蒸時間経過すると、前記排蒸弁を閉じ、
前記冷却水送り弁を開けて、前記冷却手段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する
ことを特徴とする請求項2に記載の殺菌装置。
The steaming valve and the cooling water feed valve are closed, while the steaming valve is opened, and steam from the steaming means is supplied to the heat exchanger to heat the circulating water, thereby Sterilize the processed material,
When the inside of the treatment tank is at a sterilization temperature or higher and the sterilization time has elapsed, while closing the steam supply valve, the exhaust steam valve is opened,
When the steaming time has elapsed after opening the steaming valve, the steaming valve is closed,
3. The object to be treated is cooled by opening the cooling water feed valve and supplying cooling water from the cooling means to the heat exchanger to cool the circulating water. The sterilizer described.
JP2012086816A 2012-04-05 2012-04-05 Sterilizer Active JP5907424B2 (en)

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