JP2015139383A - Sterilization device - Google Patents

Sterilization device Download PDF

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JP2015139383A
JP2015139383A JP2014012613A JP2014012613A JP2015139383A JP 2015139383 A JP2015139383 A JP 2015139383A JP 2014012613 A JP2014012613 A JP 2014012613A JP 2014012613 A JP2014012613 A JP 2014012613A JP 2015139383 A JP2015139383 A JP 2015139383A
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heat exchanger
water
treatment tank
cooling
valve
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JP6229887B2 (en
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健司 金澤
Kenji Kanazawa
健司 金澤
暁 若狭
Akira Wakasa
暁 若狭
泰三 松川
Taizo Matsukawa
泰三 松川
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Miura Co Ltd
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  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce a number of electrically-driven proportional valves to be used for reducing cost.SOLUTION: A treatment tank 3 stores an object 2 to be treated and water. Circulation means 9 makes stored water in the treatment tank 3 between a heat exchanger 8. On a circulation path 14, a bypass path 15 connecting front and rear parts of the heat exchanger 8, is provided. A distribution ratio of the water from the treatment tank 3 to be returned to the treatment tank 3 via the heat exchanger 8 and the water to be returned to the treatment tank 3 via the bypass path 15, can be adjusted by a cross valve 27. Steam supply means 10 supplies steam to the heat exchanger 8 for heating the circulation water by circulated the circulation means 9. Cooling means 11 supplies cooling water to the heat exchanger 8 for cooling the water circulated by the circulation means 9. The steam supply means 10 has a steam supply valve 29 for switching presence/absence of steam supply to a steam supply path 28 toward the heat exchanger, by on-off. In a sterilization step, in a state that the steam supply valve 29 is opened, the cross valve 27 is controlled based on temperature in the treatment tank 3.

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.

出願人は、先に、下記特許文献1に開示される殺菌装置を提案している。この殺菌装置では、処理槽(12)内に被処理物を収容すると共に水を貯留し、この貯留水を熱交換器(26)との間で循環させ、この循環水を熱交換器(26)において蒸気供給回路(28)からの蒸気により加熱するか、冷却水供給回路(32)からの冷却水で冷却するかを切り替えて、被処理物の加熱殺菌とその後の冷却を図る。   The applicant has previously proposed a sterilizer disclosed in Patent Document 1 below. In this sterilizer, the object to be treated is stored in the treatment tank (12) and water is stored. The stored water is circulated with the heat exchanger (26), and the circulating water is circulated to the heat exchanger (26). ) To switch between heating with the steam from the steam supply circuit (28) or cooling with the cooling water from the cooling water supply circuit (32), and heat sterilization of the object to be processed and subsequent cooling.

殺菌工程では、循環水をバイパス路(36)に通すことなく全量熱交換器(26)に通した状態で(段落0035第1文)、処理槽(12)の制御目標温度と温度センサ(16)の検出温度との差分に基づいて、給蒸弁(2804)の開度が制御される(段落0033)。また、冷却工程では、処理槽(12)の制御目標温度と温度センサ(16)の検出温度との差分に基づいて、三方弁(42)が制御される(段落0035)。   In the sterilization process, the circulating water is not passed through the bypass passage (36), but is passed through the heat exchanger (26) (paragraph 0035, first sentence), the control target temperature of the treatment tank (12) and the temperature sensor (16). ), The opening degree of the steam supply valve (2804) is controlled (paragraph 0033). In the cooling process, the three-way valve (42) is controlled based on the difference between the control target temperature of the treatment tank (12) and the detected temperature of the temperature sensor (16) (paragraph 0035).

特開2013−9642号公報JP 2013-9642 A

従来技術では、蒸気流量調整用の給蒸弁と、バイパス流量調整用の三方弁という二つの電動比例弁を用いており、コスト高となっていた。また、構成上の問題だけでなく、制御の点においても、殺菌工程と冷却工程とで、制御する弁が異なることになる。   In the prior art, two electric proportional valves, a steam supply valve for adjusting the steam flow rate and a three-way valve for adjusting the bypass flow rate, are used, resulting in high costs. Further, not only in terms of configuration, but also in terms of control, the valves to be controlled differ between the sterilization process and the cooling process.

そこで、本発明が解決しようとする課題は、簡易な構成および制御で、コスト削減を図ることができる殺菌装置を提供することにある。   Therefore, the problem to be solved by the present invention is to provide a sterilizer capable of reducing costs 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、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、その循環路には前記熱交換器の前後を接続してバイパス路が設けられ、前記処理槽からの水を、前記熱交換器を介して前記処理槽へ戻すか、前記熱交換器を介さずに前記バイパス路を介して前記処理槽へ戻すかの分配割合を分配量調整手段で調整可能な循環手段と、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を備え、前記給蒸手段は、前記熱交換器への給蒸路に、給蒸の有無をオンオフで切り替える給蒸弁を備え、前記被処理物を加熱する殺菌工程では、前記給蒸弁を開いた状態で、前記処理槽内の温度に基づき前記分配量調整手段を制御す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. It circulates between the heat exchangers, and a bypass passage is provided in the circulation path by connecting the front and rear of the heat exchanger, and water from the treatment tank is passed to the treatment tank via the heat exchanger. In order to heat the circulating water by the circulation means that can be adjusted by the distribution amount adjusting means, the distribution ratio of whether to return to the treatment tank via the bypass path without going through the heat exchanger , Steam supply means for supplying steam to the heat exchanger, and cooling means for supplying cooling water to the heat exchanger for cooling the circulating water by the circulation means, the steam supply means, The steam supply path to the heat exchanger has a steam supply valve that switches on / off whether steam is supplied or not. The in sterilizing step of heating the object to be treated, with open the paper 蒸弁 a sterilizing apparatus and controls the distribution amount adjusting means based on the temperature of the processing bath.

請求項1に記載の発明によれば、殺菌工程では、給蒸弁を開いた状態で、処理槽内の温度に基づき分配量調整手段を制御する。これにより、熱交換器を介した循環流量を調整して、処理槽内の温度を所望に調整することができる。給蒸弁により給蒸の有無を切り替えれば足り、給蒸弁の開度を調整する必要がないので、給蒸弁としてオンオフの蒸気遮断弁を用いることができ、コストの削減を図ることができる。   According to the first aspect of the present invention, in the sterilization step, the distribution amount adjusting means is controlled based on the temperature in the processing tank with the steam supply valve opened. Thereby, the circulating flow rate via a heat exchanger can be adjusted and the temperature in a processing tank can be adjusted as desired. Since it is sufficient to switch the presence or absence of steaming with the steaming valve, it is not necessary to adjust the opening of the steaming valve, so an on / off steam shut-off valve can be used as the steaming valve, and cost can be reduced. .

請求項2に記載の発明は、前記被処理物を冷却する冷却工程では、前記給蒸弁を閉じる一方、前記熱交換器に冷却水を供給した状態で、前記処理槽内の温度に基づき前記分配量調整手段を制御す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, in the cooling step of cooling the workpiece, the steam supply valve is closed, while cooling water is supplied to the heat exchanger, based on the temperature in the processing tank. 2. The sterilizing apparatus according to claim 1, wherein the distribution amount adjusting means is controlled.

請求項2に記載の発明によれば、冷却工程では、熱交換器に冷却水を通水しつつ、処理槽内の温度に基づき分配量調整手段を制御する。これにより、熱交換器を介した循環流量を調整して、処理槽内の温度を所望に調整することができる。殺菌工程と同様に冷却工程においても、循環量調整手段を制御すれば足り、制御に統一性を持たせることができる。   According to the second aspect of the present invention, in the cooling step, the distribution amount adjusting means is controlled based on the temperature in the processing tank while passing the cooling water through the heat exchanger. Thereby, the circulating flow rate via a heat exchanger can be adjusted and the temperature in a processing tank can be adjusted as desired. Similarly to the sterilization process, it is sufficient to control the circulation amount adjusting means in the cooling process, and the control can be made uniform.

さらに、請求項3に記載の発明は、前記殺菌工程では、前記給蒸弁を開いた状態で、前記処理槽内を設定温度に維持するように前記分配量調整手段を制御し、前記殺菌工程中、前記給蒸弁を閉じた状態で、前記熱交換器に冷却水を供給して、前記設定温度を下げる操作を実行可能とされ、前記設定温度を下げる際、その温度下降速度が設定速度になるように、前記処理槽内の温度に基づき前記分配量調整手段を制御す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 sterilization step, the invention according to claim 3 controls the distribution amount adjusting means so as to maintain the inside of the treatment tank at a set temperature with the steam supply valve opened, and the sterilization step. In the state where the steam supply valve is closed, cooling water is supplied to the heat exchanger so that the operation for lowering the set temperature can be performed. When the set temperature is lowered, the temperature decreasing speed is set to the set speed. The disinfection apparatus according to claim 1 or 2, wherein the distribution amount adjusting means is controlled based on the temperature in the processing tank.

請求項3に記載の発明によれば、殺菌工程の途中で、熱交換器において循環水を冷却することで、設定温度を下げることができる。そのため、実際の調理において、最初は強火で加熱した後、中火や弱火に変えることがあるように、レトルト食品などの殺菌を兼ねた調理においても、設定温度を途中で下げることができる。しかも、設定温度を下げる際、その温度下降速度を所望に調整することができる。このようにして、被処理物に応じた最適な温度制御が可能となり、たとえば、食材の味、仕上がりの向上が期待できる。さらに、温度変化を所望に設定して、食味を落とさずに、殺菌時間の短縮を図ることも可能となる。   According to invention of Claim 3, preset temperature can be lowered | hung by cooling circulating water in a heat exchanger in the middle of a sterilization process. Therefore, in actual cooking, the set temperature can be lowered in the middle of cooking that also serves as sterilization of retort foods, etc. so that it may be heated to a medium heat or a low heat after first being heated with a high heat. In addition, when the set temperature is lowered, the temperature drop rate can be adjusted as desired. In this way, optimal temperature control according to the object to be processed becomes possible, and for example, improvement in the taste and finish of the food can be expected. Furthermore, it is possible to shorten the sterilization time without degrading the taste by setting the temperature change as desired.

本発明によれば、簡易な構成および制御で、コスト削減を図ることができる殺菌装置を実現することができる。   ADVANTAGE OF THE INVENTION According to this invention, the sterilizer which can aim at cost reduction by simple structure and control is realizable.

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、これら各手段4〜7,9〜12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) and a control means (not shown) for controlling these means 4 to 7 and 9 to 12 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13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13は、処理槽3ではなく、場合により、後述する循環路14(特にバイパス路15との合流部よりも下流側)に設けられてもよい。   The processing tank 3 is provided with a temperature sensor 13 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 13 may be provided not in the processing tank 3 but in a circulation path 14 described later (in particular, on the downstream side of the junction with the bypass path 15).

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。   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.

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14と循環ポンプ25とを備える。循環路14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14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 14 and a circulation pump 25. One end of the circulation path 14 is connected to the bottom of the treatment tank 3, and the circulation path 14 from the bottom of the treatment tank 3 is sequentially passed through the circulation pump 25 and the heat exchanger 8, and the other end is connected to the treatment 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.

循環路14には、熱交換器8の前後を接続するように、バイパス路15が設けられる。また、循環路14とバイパス路15との分岐部に、分配量調整手段としての三方弁27が設けられる。この三方弁27を制御することで、循環ポンプ25からの循環水を、熱交換器8を介して処理槽3へ戻すか、熱交換器8を介さずにバイパス路15を介して処理槽3へ戻すかの分配割合を調整することができる。   A bypass path 15 is provided in the circulation path 14 so as to connect the front and rear of the heat exchanger 8. Further, a three-way valve 27 as a distribution amount adjusting means is provided at a branch portion between the circulation path 14 and the bypass path 15. By controlling the three-way valve 27, the circulating water from the circulation pump 25 is returned to the treatment tank 3 via the heat exchanger 8, or via the bypass path 15 without the heat exchanger 8. The distribution ratio of returning to can be adjusted.

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28を備え、この給蒸路28には給蒸弁29が設けられている。給蒸弁29は、開閉のみ可能で、開度調整不能な弁で足りる。つまり、給蒸弁29は、熱交換器8への給蒸の有無をオンオフで切り替える弁である。本実施例では、エア駆動バルブから構成される。   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 28 that supplies steam from the boiler to the heat exchanger 8, and a steam supply valve 29 is provided in the steam supply path 28. The steam supply valve 29 can be opened and closed only, and a valve whose opening degree cannot be adjusted is sufficient. That is, the steam supply valve 29 is a valve that switches on / off whether or not steam is supplied to the heat exchanger 8. In this embodiment, it is composed of an air drive valve.

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30を備え、クーリングタワー30にて冷却された水は、送水ポンプ31により、冷却水送り路32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33を介してクーリングタワー30へ戻される。図示例の場合、冷却水送り路32と給蒸路28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 30, and the water cooled by the cooling tower 30 is supplied to the heat exchanger 8 via the cooling water feed path 32 by the water pump 31, and the water after passing through the heat exchanger 8. Is returned to the cooling tower 30 via the cooling water return path 33. In the case of the illustrated example, the cooling water feed path 32 and the steam supply path 28 are a common pipe line on the heat exchanger 8 side.

冷却水送り路32には冷却水送り弁34が設けられる一方、冷却水戻し路33には冷却水戻し弁35が設けられている。冷却水送り路32と給蒸路28との合流部は、冷却水送り弁34や給蒸弁29より下流側(熱交換器8側)に配置されている。   A cooling water feed valve 34 is provided in the cooling water feed path 32, while a cooling water return valve 35 is provided in the cooling water return path 33. The junction between the cooling water feed path 32 and the steam supply path 28 is disposed downstream (on the heat exchanger 8 side) from the cooling water feed valve 34 and the steam supply valve 29.

冷却水送り弁34および冷却水戻し弁35を開いた状態で、送水ポンプ31を作動させると、クーリングタワー30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34および冷却水戻し弁35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 31 is operated with the cooling water feed valve 34 and the cooling water return valve 35 opened, the cooling water can be circulated between the cooling tower 30 and the heat exchanger 8. On the other hand, if the cooling water feed valve 34 and the cooling water return valve 35 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33の内、冷却水戻し弁35より上流側(熱交換器8側)に設けられ、冷却水戻し路33から分岐するドレン排出路36に、ドレン排出弁37、スチームトラップ38および逆止弁39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37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 coolant return valve 35 (on the heat exchanger 8 side) in the coolant return path 33, and is connected to a drain discharge path 36 that branches from the coolant return path 33. 37, a steam trap 38 and a check valve 39 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 37.

制御手段は、温度センサ13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4〜7,9〜12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、三方弁27、給蒸弁29、クーリングタワー30、送水ポンプ31、冷却水送り弁34、冷却水戻し弁35、ドレン排出弁37の他、温度センサ13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 12 based on the elapsed time as well as the detection signals of the temperature sensor 13 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 three-way valve 27, the steam supply valve 29, the cooling tower 30, the water supply pump 31, and the cooling water supply valve 34. In addition to the cooling water return valve 35 and the drain discharge valve 37, the temperature sensor 13 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18,20,22,29,34,35,37は閉じられており、各ポンプ17,25,31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, 29, 34, 35, 37 are closed, and the pumps 17, 25, 31 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内の温度を設定温度(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。この際、三方弁27は、循環ポンプ25からの循環水を全量、熱交換器8に通す状態に維持すれば足りる。また、移行工程では、冷却水送り弁34および冷却水戻し弁35を閉じる一方、給蒸弁29およびドレン排出弁37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37を開けておくことで、蒸気の凝縮水は、スチームトラップ38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 set temperature (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. At this time, it is sufficient for the three-way valve 27 to maintain the entire amount of circulating water from the circulation pump 25 so as to pass through the heat exchanger 8. In the transition process, the cooling water feed valve 34 and the cooling water return valve 35 are closed, while the steam supply valve 29 and the drain discharge valve 37 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 37, the condensed water of the steam is discharged through the steam trap 38.

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内が設定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 pressurization in the treatment tank 3 by the pressurizing means 6 is continued until the end of the cooling step to a pressure higher than the saturated vapor pressure corresponding to the temperature in the treatment tank even after the inside of the treatment tank 3 rises to the set temperature. The

≪(3)殺菌工程≫
殺菌工程では、処理槽3内の温度を設定温度に保持して、被処理物2を加熱して殺菌する。具体的には、給蒸弁29およびドレン排出弁37を開いた状態に維持すると共に、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13の検出温度を設定温度に維持するように、三方弁27の開度を調整する。つまり、温度センサ13の検出温度を設定温度に維持するように、熱交換器8への循環水の通水流量を調整する。処理槽3内が設定温度以上で設定時間経過すると、給蒸弁29およびドレン排出弁37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 process, the temperature in the processing tank 3 is maintained at a set temperature, and the workpiece 2 is heated and sterilized. Specifically, the steam supply valve 29 and the drain discharge valve 37 are maintained in an open state, and the temperature detected by the temperature sensor 13 is maintained at the set temperature while circulating the water stored in the treatment tank 3 by the circulation means 9. Thus, the opening degree of the three-way valve 27 is adjusted. That is, the flow rate of circulating water to the heat exchanger 8 is adjusted so that the temperature detected by the temperature sensor 13 is maintained at the set temperature. When the set time elapses above the set temperature in the processing tank 3, the steam supply valve 29 and the drain discharge valve 37 are closed to stop the steam supply to the heat exchanger 8, and the sterilization process is ended.

殺菌工程中、設定温度を、上げたり、下げたりすることができる。たとえば、殺菌工程において、第一設定温度で第一設定時間維持した後、第一設定温度よりも高い第二設定温度にまで温度を上げ(または第一設定温度よりも低い第二設定温度にまで温度を下げ)、その第二設定温度で第二設定時間維持することができる。なお、設定温度は、二段階に限らず、三段階以上に変更してもよい。   The set temperature can be raised or lowered during the sterilization process. For example, in the sterilization process, after maintaining the first set time at the first set temperature, the temperature is increased to a second set temperature higher than the first set temperature (or to a second set temperature lower than the first set temperature). The temperature can be lowered) and maintained at the second set temperature for a second set time. The set temperature is not limited to two stages, and may be changed to three or more stages.

設定温度を上げるには、温度センサ13の検出温度に基づき、三方弁27を制御すればよい。通常、前記移行工程と同様に、給蒸弁29およびドレン排出弁37を開いた状態で、循環ポンプ25からの循環水を全量、熱交換器8に通すように三方弁27を制御する。   In order to increase the set temperature, the three-way valve 27 may be controlled based on the temperature detected by the temperature sensor 13. Normally, the three-way valve 27 is controlled so that the entire amount of circulating water from the circulation pump 25 is passed through the heat exchanger 8 with the steam supply valve 29 and the drain discharge valve 37 open, as in the transition step.

設定温度を下げるには、給蒸手段10による加熱を停止した状態で、後述する冷却工程と同様に、熱交換器8において冷却手段11により循環水を冷却すればよい。具体的には、給蒸弁29およびドレン排出弁37を閉じる一方、冷却水送り弁34および冷却水戻し弁35を開いた状態で、クーリングタワー30および送水ポンプ31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、三方弁27を制御して、熱交換器8への循環水の通水流量を調整して、処理槽3内の温度を所望に下げることができる。   In order to lower the set temperature, the circulating water may be cooled by the cooling means 11 in the heat exchanger 8 in the state where the heating by the steam supply means 10 is stopped, as in the cooling step described later. Specifically, the steam supply valve 29 and the drain discharge valve 37 are closed, while the cooling water feed valve 34 and the cooling water return valve 35 are opened, the cooling tower 30 and the water feed pump 31 are operated, and the heat exchanger 8 Cooling water may be circulated in the tank. At this time, the three-way valve 27 is controlled to adjust the flow rate of circulating water to the heat exchanger 8 so that the temperature in the treatment tank 3 can be lowered as desired.

なお、処理槽3内の温度を下げる際、その温度下降速度が設定速度になるように、熱交換器8に通す循環水の流量を調整するのが好ましい。具体的には、温度センサ13の検出温度を監視しつつ、設定速度で温度が低下するように、三方弁27の開度を調整すればよい。設定温度が目標温度まで下がれば、その設定温度を維持するように、三方弁27の開度を調整すればよい。   In addition, when lowering | hanging the temperature in the processing tank 3, it is preferable to adjust the flow volume of the circulating water passed through the heat exchanger 8 so that the temperature decreasing speed may become a setting speed. Specifically, the opening degree of the three-way valve 27 may be adjusted so that the temperature decreases at a set speed while monitoring the temperature detected by the temperature sensor 13. If the set temperature falls to the target temperature, the opening degree of the three-way valve 27 may be adjusted so as to maintain the set temperature.

このようにして、殺菌工程の途中で、所望により設定温度を上げたり下げたりすることができる。そのため、被処理物2に応じた最適な温度制御が可能となる。特に、被処理物2に合わせて、殺菌初期に高温で殺菌して、その後に設定温度を下げるといった運転が可能となる。つまり、設定温度を途中で下げることで、あたかも、最初は強火で加熱した後、中火や弱火に変えて加熱する処理が可能となる。これにより、食材の味、仕上がりの向上が期待できる。また、たとえば、従来、80℃でX分だけ要していた殺菌を、100℃でY分と80℃でZ分(但しX>Y+Z)というように、殺菌時間を短くしつつ、食味を落とさずに調理することが可能となる。   In this way, the set temperature can be raised or lowered as desired during the sterilization process. Therefore, optimum temperature control according to the workpiece 2 is possible. In particular, in accordance with the object to be treated 2, it is possible to perform an operation in which sterilization is performed at a high temperature at the initial stage of sterilization and then the set temperature is lowered. In other words, by lowering the set temperature in the middle, it is possible to perform a process of heating by changing to medium heat or low heat after first heating with high heat. Thereby, the improvement of the taste of a foodstuff and a finish can be expected. Also, for example, sterilization, which conventionally required X minutes at 80 ° C., reduces the taste while shortening the sterilization time, such as Y minutes at 100 ° C. and Z minutes at 80 ° C. (X> Y + Z). It becomes possible to cook without.

ところで、殺菌工程中、万一、温度センサ13の検出温度が上限温度を超えると、給蒸弁29を閉じるのが好ましい。この場合、その後、温度センサ13の検出温度が、前記上限温度よりも低い所定温度まで下がれば、再び給蒸弁29を開けばよい。   Incidentally, during the sterilization process, if the temperature detected by the temperature sensor 13 exceeds the upper limit temperature, the steam supply valve 29 is preferably closed. In this case, after that, if the temperature detected by the temperature sensor 13 falls to a predetermined temperature lower than the upper limit temperature, the steam supply valve 29 may be opened again.

≪(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29およびドレン排出弁37を閉じる一方、冷却水送り弁34および冷却水戻し弁35を開けた状態で、クーリングタワー30および送水ポンプ31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. Further, during this circulation, the steam supply valve 29 and the drain discharge valve 37 are closed, while the cooling water feed valve 34 and the cooling water return valve 35 are opened, the cooling tower 30 and the water feed pump 31 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。   When the cooling time elapses from the start of the cooling process, the temperature in the treatment tank 3 falls below the cooling temperature, or when a predetermined time elapses after the cooling temperature falls, the cooling means 11 supplies the cooling water to the heat exchanger. Stop and end 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.

冷却工程では、温度センサ13の検出温度に基づき三方弁27を制御して、循環水の熱交換器8への通水量を調整して、処理槽3内の温度を調整することができる。これにより、熱交換器8に供給される冷却水の水温の変化にも対応して、処理槽3内の温度を所定に調整しつつ下げることができる。また、冷却工程では、殺菌工程における設定温度を下げる際と同様に、温度下降速度が設定速度になるように、三方弁27を制御してもよい。なお、時間経過に伴い、温度下降速度を変更して、処理槽3内の温度を所望に下げるように制御してもよい。   In the cooling step, the three-way valve 27 is controlled based on the temperature detected by the temperature sensor 13 to adjust the amount of water flowing into the heat exchanger 8 of the circulating water, thereby adjusting the temperature in the treatment tank 3. Thereby, the temperature in the processing tank 3 can be lowered while adjusting to a predetermined value in response to a change in the temperature of the cooling water supplied to the heat exchanger 8. Further, in the cooling process, the three-way valve 27 may be controlled so that the temperature lowering speed becomes the set speed as in the case of lowering the set temperature in the sterilization process. In addition, you may control so that the temperature in the processing tank 3 may be lowered | hung as desired by changing a temperature fall rate with time passage.

≪(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 pressurization 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 can be taken out from the processing tank 3. it can.

本実施例の殺菌装置1によれば、三方弁27のみが開度調整され、その他の弁は開閉が切り替えられる。そのため、構成および制御が容易となる。ところで、熱交換器8への循環水の通水量を調整するために、仮に循環ポンプ25をインバータ制御した場合には、ノズル26からの噴霧量が変化し、場合によってはノズル26からの噴霧が行えないおそれがある。ところが、本実施例の殺菌装置1では、全体の循環流量は所望に維持され、バイパス流量を調整するので、ノズル26から被処理物2への噴射を所望に維持することができる。   According to the sterilizer 1 of the present embodiment, only the three-way valve 27 is adjusted in opening, and the other valves are switched between open and closed. Therefore, the configuration and control become easy. By the way, if the circulation pump 25 is inverter-controlled to adjust the amount of circulating water flowing to the heat exchanger 8, the amount of spray from the nozzle 26 changes, and in some cases, the spray from the nozzle 26 is sprayed. May not be possible. However, in the sterilization apparatus 1 of the present embodiment, the entire circulation flow rate is maintained as desired, and the bypass flow rate is adjusted, so that the injection from the nozzle 26 to the workpiece 2 can be maintained as desired.

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。たとえば、前記実施例では、分配量調整手段として、循環路14とバイパス路15との分岐部に三方弁27を設置したが、バイパス路15との分岐部と合流部との間の循環路14(特にバイパス路15との分岐部と熱交換器8との間)に開度調整可能な弁(開度調整弁)を設けてもよい。その場合、バイパス路15には、開閉のみ可能な弁(開閉弁)を設けておくのが好ましい。そして、熱交換器8への循環水の通水流量を調整するには、開閉弁を開いた状態で、開度調整弁の開度を調整すればよい。   The sterilization apparatus 1 of the present invention is not limited to the configuration of the above embodiment, and can be changed as appropriate. For example, in the above-described embodiment, the three-way valve 27 is installed at the branch portion between the circulation path 14 and the bypass path 15 as the distribution amount adjusting means, but the circulation path 14 between the branch section with the bypass path 15 and the junction section. A valve (opening adjustment valve) capable of adjusting the opening degree may be provided (particularly between the branch portion with the bypass passage 15 and the heat exchanger 8). In that case, the bypass passage 15 is preferably provided with a valve (open / close valve) that can only be opened and closed. And in order to adjust the flow volume of the circulating water to the heat exchanger 8, what is necessary is just to adjust the opening degree of an opening degree adjustment valve in the state which opened the on-off valve.

あるいは、これとは逆に、バイパス路15に開度調整可能な弁(開度調整弁)を設けてもよい。その場合、バイパス路15との分岐部と合流部との間の循環路14(特にバイパス路15との分岐部と熱交換器8との間)には、開閉のみ可能な弁(開閉弁)を設けておくのが好ましい。そして、熱交換器8への循環水の通水流量を調整するには、開閉弁を開いた状態で、開度調整弁の開度を調整すればよい。   Alternatively, conversely, a valve (opening adjustment valve) capable of adjusting the opening degree may be provided in the bypass passage 15. In that case, a valve (open / close valve) that can only be opened and closed in the circulation path 14 (particularly between the branch section with the bypass path 15 and the heat exchanger 8) between the branch section with the bypass path 15 and the junction section. Is preferably provided. And in order to adjust the flow volume of the circulating water to the heat exchanger 8, what is necessary is just to adjust the opening degree of an opening degree adjustment valve in the state which opened the on-off valve.

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、殺菌工程では、給蒸弁29を開いた状態に維持して、三方弁27などを制御すればよい。また、冷却工程では、熱交換器8に冷却水を通しつつ、三方弁27などを制御すればよい。   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. In the sterilization process, the three-way valve 27 and the like may be controlled while keeping the steam supply valve 29 open. In the cooling process, the three-way valve 27 and the like may be controlled while passing cooling water through the heat exchanger 8.

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 温度センサ
14 循環路
15 バイパス路
25 循環ポンプ
27 三方弁(分配量調整手段)
28 給蒸路
29 給蒸弁
30 クーリングタワー
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 Temperature sensor 14 Circulation path 15 Bypass path 25 Circulating pump 27 Three-way valve (Distribution amount adjusting means)
28 Steam supply path 29 Steam supply valve 30 Cooling tower

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、その循環路には前記熱交換器の前後を接続してバイパス路が設けられ、前記処理槽からの水を、前記熱交換器を介して前記処理槽へ戻すか、前記熱交換器を介さずに前記バイパス路を介して前記処理槽へ戻すかの分配割合を分配量調整手段で調整可能な循環手段と、
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を備え、
前記給蒸手段は、前記熱交換器への給蒸路に、給蒸の有無をオンオフで切り替える給蒸弁を備え、
前記被処理物を加熱する殺菌工程では、前記給蒸弁を開いた状態で、前記処理槽内の温度に基づき前記分配量調整手段を制御する
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;
The stored water in the treatment tank is circulated with the heat exchanger, and a bypass path is provided in the circulation path before and after the heat exchanger, and water from the treatment tank is exchanged with the heat exchanger. A circulation means capable of adjusting a distribution ratio of whether to return to the treatment tank via a vessel or to return to the treatment tank via the bypass without going through the heat exchanger,
In order to heat the circulating water by the circulation means, steam supply means for supplying steam to the heat exchanger,
A cooling means for supplying cooling water to the heat exchanger in order to cool the circulating water by the circulation means,
The steaming means comprises a steaming valve that switches on / off the presence or absence of steaming in the steaming path to the heat exchanger,
In the sterilization step of heating the object to be processed, the distribution amount adjusting means is controlled based on the temperature in the processing tank with the steam supply valve opened.
前記被処理物を冷却する冷却工程では、前記給蒸弁を閉じる一方、前記熱交換器に冷却水を供給した状態で、前記処理槽内の温度に基づき前記分配量調整手段を制御する
ことを特徴とする請求項1に記載の殺菌装置。
In the cooling step of cooling the object to be treated, the distribution amount adjusting means is controlled based on the temperature in the treatment tank while the cooling valve is closed and the cooling water is supplied to the heat exchanger. The sterilizer according to claim 1, wherein
前記殺菌工程では、前記給蒸弁を開いた状態で、前記処理槽内を設定温度に維持するように前記分配量調整手段を制御し、
前記殺菌工程中、前記給蒸弁を閉じた状態で、前記熱交換器に冷却水を供給して、前記設定温度を下げる操作を実行可能とされ、
前記設定温度を下げる際、その温度下降速度が設定速度になるように、前記処理槽内の温度に基づき前記分配量調整手段を制御する
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 sterilization step, with the steam supply valve opened, the distribution amount adjusting means is controlled so as to maintain the inside of the processing tank at a set temperature,
During the sterilization process, with the steam supply valve closed, cooling water is supplied to the heat exchanger, and an operation for lowering the set temperature can be performed.
The distribution amount adjusting means is controlled based on the temperature in the processing tank so that the temperature decreasing speed becomes a set speed when the set temperature is lowered. Sterilizer.
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JP2021058122A (en) * 2019-10-04 2021-04-15 三浦工業株式会社 Sterilizer

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CN109704424A (en) * 2018-12-29 2019-05-03 楚天科技股份有限公司 A kind of on-line checking, sterilizing water distribution system and method for supplying water

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JP2020124189A (en) * 2019-01-31 2020-08-20 株式会社井上鉄工所 Heat sterilization apparatus
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