JP2023119243A - Processing device - Google Patents

Processing device Download PDF

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JP2023119243A
JP2023119243A JP2022022027A JP2022022027A JP2023119243A JP 2023119243 A JP2023119243 A JP 2023119243A JP 2022022027 A JP2022022027 A JP 2022022027A JP 2022022027 A JP2022022027 A JP 2022022027A JP 2023119243 A JP2023119243 A JP 2023119243A
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water
cooling
heat exchanger
abnormality
treated water
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大祐 駒井
Daisuke Komai
雅夫 蔵野
Masao Kurano
泰三 松川
Taizo Matsukawa
光央 櫛部
Mitsuhisa Kushibe
康 田中
Yasushi Tanaka
琢也 桝田
Takuya Masuda
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Miura Co Ltd
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Miura Co Ltd
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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)

Abstract

To provide a processing device capable of monitoring a cooling state of process water in a heat exchanger and cooling the process water in an auxiliary manner in a case where abnormality of cooling occurs.SOLUTION: The present invention relates to a processing device 1 comprising a processing tub 3, a heat exchanger 9, abnormality detection means 16 and auxiliary cooling means 4. Provided is the processing device 1 in which the processing tub 3 heats or cools an internally accommodated processed object 2 by process water circulating between the processing tub 3 and the heat exchanger 9, the heat exchanger 9 cools the process water by heat exchange between the process water and a fluid, the abnormality detection means 16 detects abnormality of cooling in the heat exchanger 9 based on a state amount change of the process water or the fluid before/after the heat exchange or based on a flow rate of the fluid, and the auxiliary cooling means 4 cools the process water in a case where abnormality is detected.SELECTED DRAWING: Figure 1

Description

本発明は、被処理物の加熱処理や冷却処理に用いられる処理装置に関するものである。 BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a processing apparatus used for heating and cooling an object to be processed.

食品の殺菌等を目的として、被処理物を処理槽に収容し、処理槽と熱交換器との間で循環する処理水により被処理物を加熱後に冷却する処理装置が用いられている。特許文献1には、熱交換器に蒸気を供給することで加熱した処理水により被処理物を加熱殺菌し、クーリングタワーから熱交換器に冷却水を供給することで冷却した処理水により被処理物を冷却することが可能な、食品の加熱殺菌用の処理装置が開示されている。 2. Description of the Related Art For the purpose of food sterilization, etc., a treatment apparatus is used in which an object to be treated is placed in a treatment tank, heated by treated water circulating between the treatment tank and a heat exchanger, and then cooled. In Patent Document 1, the object to be treated is sterilized by heating with the treated water heated by supplying steam to the heat exchanger, and the object to be treated is cooled by supplying cooling water from the cooling tower to the heat exchanger. Disclosed is a processing apparatus for heat sterilization of foodstuffs capable of cooling the

特許第4229420号公報Japanese Patent No. 4229420

このような処理装置においては、クーリングタワー等の冷却手段から熱交換器への冷却水の供給が滞ると、処理槽内の冷却が不十分となる。特に被処理物が食品である場合には、冷却が不十分であると過加熱による品質不良が生じやすい。熱交換器における処理水の冷却状態を監視することができれば、冷却の異常が発生した場合に早期に適切な対応を行うことができる。 In such a processing apparatus, if the supply of cooling water from a cooling means such as a cooling tower to the heat exchanger is interrupted, the cooling inside the processing tank becomes insufficient. In particular, when the object to be processed is food, insufficient cooling tends to result in poor quality due to overheating. If it is possible to monitor the cooling state of the treated water in the heat exchanger, it is possible to promptly take appropriate measures when a cooling abnormality occurs.

本発明はこのような事情に鑑みてなされたものであり、熱交換器における処理水の冷却状態を監視するとともに、冷却の異常が発生した場合に処理水を補助的に冷却することが可能な処理装置を提供することを目的とする。 The present invention has been made in view of such circumstances, and it is possible to monitor the cooling state of the treated water in the heat exchanger and to auxiliary cool the treated water when a cooling abnormality occurs. It is an object of the present invention to provide a processing apparatus.

本発明によれば、処理装置であって、処理槽と、熱交換器と、異常検出手段と、補助冷却手段とを備え、前記処理槽は、内部に収容された被処理物を、前記処理槽と前記熱交換器との間を循環する処理水により加熱又は冷却するよう構成され、前記熱交換器は、前記処理水と流体との間の熱交換により前記処理水を冷却するよう構成され、前記異常検出手段は、前記処理水又は前記流体の熱交換前後の状態量変化に基づき、又は前記流体の流量に基づき、前記熱交換器における冷却の異常を検出するよう構成され、前記補助冷却手段は、前記異常が検出された場合に前記処理水を冷却するよう構成される、処理装置が提供される。 According to the present invention, the processing apparatus comprises a processing tank, a heat exchanger, an abnormality detection means, and an auxiliary cooling means. configured to be heated or cooled by treated water circulating between a tank and said heat exchanger, said heat exchanger configured to cool said treated water by heat exchange between said treated water and a fluid; The abnormality detection means is configured to detect a cooling abnormality in the heat exchanger based on a state quantity change before and after heat exchange of the treated water or the fluid, or based on the flow rate of the fluid, and the auxiliary cooling Means are provided for a treatment unit configured to cool the treated water when the anomaly is detected.

本発明に係る処理装置においては、異常検出手段により処理水又は流体の熱交換前後の状態量変化を監視することで、熱交換器における冷却の異常を検出することが可能である。また、異常が検出された場合には、補助冷却手段が処理水を補助的に冷却し、被処理物の過加熱を回避することができる。 In the processing apparatus according to the present invention, it is possible to detect a cooling abnormality in the heat exchanger by monitoring the state quantity change of the treated water or fluid before and after the heat exchange by the abnormality detection means. Further, when an abnormality is detected, the auxiliary cooling means can auxiliary cool the treated water to avoid overheating of the object to be treated.

以下、本発明の種々の実施形態を例示する。以下に示す実施形態は互いに組み合わせ可能である。
好ましくは、前記異常検出手段は、前記流体の熱交換前後の圧力差に基づき前記異常を検出するよう構成される。
好ましくは、前記異常検出手段は、前記処理水の熱交換前後の温度差に基づき前記異常を検出するよう構成される。
好ましくは、前記異常検出手段は、前記流体の熱交換前後の温度差に基づき前記異常を検出するよう構成される。
好ましくは、前記補助冷却手段は、前記処理槽、又は前記処理水の循環路に前記処理水を供給するよう構成された給水手段であり、前記給水手段は、前記異常が検出された場合に前記処理水を追加で供給するよう構成される。
好ましくは、主冷却手段を備え、前記主冷却手段は、前記熱交換器に前記流体としての第1冷却水を供給するよう構成され、前記補助冷却手段は、前記異常が検出された場合に前記熱交換器に第2冷却水を供給して前記処理水を冷却するよう構成される。
Various embodiments of the present invention are illustrated below. The embodiments shown below can be combined with each other.
Preferably, the abnormality detection means is configured to detect the abnormality based on a pressure difference before and after heat exchange of the fluid.
Preferably, the abnormality detection means is configured to detect the abnormality based on a temperature difference between before and after heat exchange of the treated water.
Preferably, the abnormality detection means is configured to detect the abnormality based on a temperature difference between before and after heat exchange of the fluid.
Preferably, the auxiliary cooling means is water supply means configured to supply the treated water to the treatment tank or the circulation path for the treated water, and the water supply means is adapted to supply the It is configured to additionally supply treated water.
Preferably, a main cooling means is provided, the main cooling means is configured to supply first cooling water as the fluid to the heat exchanger, and the auxiliary cooling means is adapted to reduce the A second cooling water is supplied to the heat exchanger to cool the treated water.

本発明の一実施形態に係る殺菌装置1を示す概略図である。It is a schematic diagram showing a sterilization device 1 according to an embodiment of the present invention. 図1の殺菌装置1の動作を示すフローチャートである。2 is a flow chart showing the operation of the sterilizer 1 of FIG. 1;

以下、図面を参照して本発明の実施形態について説明する。以下に示す実施形態中で示した各特徴事項は、互いに組み合わせ可能である。また、各特徴事項について独立して発明が成立する。 Embodiments of the present invention will be described below with reference to the drawings. Each feature shown in the embodiments shown below can be combined with each other. In addition, the invention is established independently for each characteristic item.

1.殺菌装置1
図1は、本発明の一実施形態に係る処理装置としての殺菌装置1を示す概略図である。本実施形態の殺菌装置1は、被処理物2を加熱殺菌し、その後冷却するための装置である。被処理物2の種類は特に問わないが、殺菌装置1は、食品、特にレトルト食品に対して好適に用いられる。
1. Sterilizer 1
FIG. 1 is a schematic diagram showing a sterilization device 1 as a processing device according to one embodiment of the present invention. The sterilization apparatus 1 of this embodiment is an apparatus for thermally sterilizing an object 2 to be processed and then cooling it. Although the type of the object 2 to be treated is not particularly limited, the sterilizer 1 is preferably used for food, especially retort food.

殺菌装置1は、処理槽3と、給水手段4と、排水手段5と、加圧手段6と、排気手段7と、循環手段8と、熱交換器9と、給蒸手段10と、主冷却手段11と、ドレン排出手段13と、制御手段15と、異常検出手段16とを備える。以下、各要素の構成を具体的に説明する。 The sterilization apparatus 1 includes a treatment tank 3, a water supply means 4, a drainage means 5, a pressurization means 6, an exhaust means 7, a circulation means 8, a heat exchanger 9, a steam supply means 10, and a main cooling means. Means 11 , drain discharge means 13 , control means 15 and abnormality detection means 16 are provided. The configuration of each element will be specifically described below.

処理槽3は、被処理物2を収容する中空容器であり、内部に収容された被処理物2を、処理槽3と熱交換器9との間を循環する処理水により加熱又は冷却するように構成される。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。本実施形態において、被処理物2は、処理槽3内において台車上に複数段に亘って収容されたトレー20に載置され、処理槽3内の底面よりも上方において加熱殺菌処理がなされる。 The processing tank 3 is a hollow container containing the object 2 to be processed, and the object 2 to be processed contained therein is heated or cooled by the treated water circulating between the processing tank 3 and the heat exchanger 9 . configured to Although the shape of the processing tank 3 is not particularly limited, in this embodiment, the processing tank 3 is provided with a horizontally arranged cylindrical member. It is possible. Therefore, by opening the door, the object to be processed 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 airtightly closed. In this embodiment, the object 2 to be treated is placed on trays 20 accommodated over a plurality of stages on a carriage in the treatment tank 3, and heat sterilization is performed above the bottom surface in the treatment tank 3. .

処理槽3には、処理槽3内の温度を検出する温度センサ(図示省略)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。水位検出器は、その構成を特に問わないが、たとえば電極式水位検出器とされる。 The processing bath 3 is provided with a temperature sensor (not shown) for detecting the temperature inside the processing bath 3 and a water level detector (not shown) for detecting the water level inside the processing bath 3 . The water level detector may have any configuration, but may be an electrode type water level detector, for example.

給水手段4は、処理槽3の底部に接続された給水路40を介して、処理槽3内へ水を供給する。給水路40には、給水ポンプ41と給水弁42とが設けられている。給水ポンプ41を作動させた状態で給水弁42を開くことで、給水源(図示省略)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。本実施形態では、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 processing bath 3 through a water supply channel 40 connected to the bottom of the processing bath 3 . A water supply pump 41 and a water supply valve 42 are provided in the water supply path 40 . By opening the water supply valve 42 while the water supply pump 41 is in operation, water from a water supply source (not shown) can be supplied into the processing tank 3 and stored in the processing tank 3 . In this embodiment, water is stored in the processing bath 3 up to a set water level at which the objects 2 to be processed stored in the processing bath 3 are not immersed.

本実施形態の給水手段4は、補助冷却手段としての機能も有する。後述する異常検出手段16により熱交換器9における処理水の冷却の異常が検出されると、給水手段4から処理槽3内へ追加で比較的低温の水を供給する。これにより、処理槽3内の温度が比較的高温の状態で保持されることを防ぎ、被処理物2を冷却することができる。 The water supply means 4 of this embodiment also functions as an auxiliary cooling means. When an abnormality in cooling of the treated water in the heat exchanger 9 is detected by the abnormality detection means 16, which will be described later, relatively low-temperature water is additionally supplied from the water supply means 4 into the treatment tank 3. FIG. As a result, it is possible to prevent the temperature inside the processing tank 3 from being maintained at a relatively high temperature, and to cool the object 2 to be processed.

排水手段5は、処理槽3の底部に接続された排水路50を介して、処理槽3内から水を排出する。排水路50には、排水弁51及び逆止弁52が設けられている。排水弁51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 drains water from the treatment tank 3 through a drainage channel 50 connected to the bottom of the treatment tank 3 . The drainage channel 50 is provided with a drainage valve 51 and a check valve 52 . By opening the drain valve 51, the water in the treatment tank 3 can be discharged to the outside.

加圧手段6は、加圧路60を介して処理槽3内へ加圧空気(圧縮空気)を供給する。加圧路60に設けられた加圧弁61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 means 6 supplies pressurized air (compressed air) into the processing tank 3 through the pressurizing passage 60 . By opening the pressurization valve 61 provided in the pressurization path 60, the pressurized air from the pressurized air source can be supplied into the processing bath 3 to pressurize the inside of the processing bath 3 to a pressure exceeding the atmospheric pressure. can.

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70を介して気体を排出する。排気路70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71と逆止弁72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71を開くと、処理槽3内の気体は排気路70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 gas through the exhaust path 70 from the inside of the processing tank 3 under pressure exceeding the atmospheric pressure. The exhaust path 70 is connected to the upper portion of the processing bath 3, and is provided with an exhaust valve 71 and a check valve 72 in order from the processing bath 3 side. When the exhaust valve 71 is opened while the pressure in the processing tank 3 exceeds the atmospheric pressure, the gas in the processing tank 3 is discharged to the outside through the exhaust path 70, and the pressure in the processing tank 3 can be lowered. can.

循環手段8は、処理槽3と熱交換器9との間で処理水を循環させる。循環手段8は、循環路80と、循環ポンプ81と、噴出ノズル82とを備える。循環路80は、一端部が処理槽3の底部に接続され、循環ポンプ81と熱交換器9とを順に介して、他端部が処理槽3内の噴出ノズル82に接続されている。噴出ノズル82は、循環路80からの処理水を被処理物2へ向けて噴射する。噴出ノズル82の形状及び数は任意であるが、処理槽3に収容された被処理物2の上部に満遍なく処理水が噴出されるよう構成することが好ましい。 The circulation means 8 circulates the treated water between the treatment tank 3 and the heat exchanger 9 . The circulation means 8 includes a circulation path 80 , a circulation pump 81 and an ejection nozzle 82 . One end of the circulation path 80 is connected to the bottom of the processing bath 3 , and the other end is connected to a jet nozzle 82 in the processing bath 3 via the circulation pump 81 and the heat exchanger 9 in this order. The jet nozzle 82 jets the treated water from the circulation path 80 toward the object 2 to be treated. The shape and number of the jet nozzles 82 are arbitrary, but it is preferable to configure them so that the treated water is evenly jetted over the objects to be treated 2 contained in the treatment bath 3 .

熱交換器9は、循環手段8の循環路80の中途に設けられる。熱交換器9は、循環路80を流通する処理水を、給蒸手段10から供給される加熱蒸気との熱交換により加熱し、主冷却手段11から供給される冷却用流体としての冷水との熱交換により冷却するために用いられる。なお、以下の説明において、給蒸手段10から供給される蒸気や主冷却手段11から供給される冷却水が流通する側を熱交換器9の一次側、循環路80と接続されて処理水が流通する側を熱交換器9の二次側と呼ぶ。 The heat exchanger 9 is provided in the middle of the circulation path 80 of the circulation means 8 . The heat exchanger 9 heats the treated water flowing through the circulation path 80 by heat exchange with the heating steam supplied from the steam supply means 10, and heats the treated water with cold water as a cooling fluid supplied from the main cooling means 11. Used for cooling by heat exchange. In the following description, the side through which the steam supplied from the steam supply means 10 and the cooling water supplied from the main cooling means 11 flow is the primary side of the heat exchanger 9, and the circuit 80 is connected to the treated water. The flowing side is called the secondary side of the heat exchanger 9 .

給蒸手段10は、熱交換器9の一次側に加熱蒸気を供給して、循環路80を流通する処理水を加熱する。給蒸手段10は、ボイラ(図示省略)からの蒸気を熱交換器9へ供給する給蒸路100を備え、給蒸路100には給蒸弁101が設けられている。給蒸弁101の開度を調整することで循環路80を循環する処理水の温度を調整可能であり、これにより処理槽3内を所望の温度に調整することができる。具体的には、処理槽3の温度センサの検出温度に基づき、給蒸弁101の開度が調整される。図示例の場合、給蒸路100は、給蒸弁101よりも下流側(熱交換器9の側)の管路の一部が主冷却手段11の冷水送り路112と共通の管路となっている。また、給蒸路100は、冷水送り弁114より下流側(熱交換器9側)の位置において冷水送り路112と合流している。 The steam supply means 10 supplies heating steam to the primary side of the heat exchanger 9 to heat the treated water flowing through the circulation path 80 . The steam supply means 10 includes a steam supply line 100 for supplying steam from a boiler (not shown) to the heat exchanger 9 , and the steam supply line 100 is provided with a steam supply valve 101 . By adjusting the opening degree of the steam supply valve 101, the temperature of the treated water circulating in the circulation path 80 can be adjusted, thereby adjusting the inside of the treatment bath 3 to a desired temperature. Specifically, the opening degree of the steam supply valve 101 is adjusted based on the temperature detected by the temperature sensor of the processing tank 3 . In the illustrated example, in the steam supply line 100, a portion of the pipeline on the downstream side (the heat exchanger 9 side) of the steam supply valve 101 is shared with the cold water feed path 112 of the main cooling means 11. ing. Also, the steam supply passage 100 joins the cold water feed passage 112 at a position downstream of the cold water feed valve 114 (on the side of the heat exchanger 9).

主冷却手段11は、熱交換器9の一次側に冷水を供給して、循環路80を流通する処理水を冷却する。主冷却手段11は、クーリングタワー110を備える。クーリングタワー110にて冷却された冷水(クーリングタワー水)は、送水ポンプ111により冷水送り路112を介して熱交換器9へ供給され、熱交換器9を通過後の水は冷水戻し路113を介してクーリングタワー110へ戻される。熱交換器9において冷却用流体としての冷水との熱交換により処理水を冷却することで、処理槽3内の温度を低下させ、被処理物2を冷却することができる。 The main cooling means 11 supplies cold water to the primary side of the heat exchanger 9 to cool the treated water flowing through the circulation path 80 . The main cooling means 11 comprises a cooling tower 110 . Chilled water (cooling tower water) cooled by the cooling tower 110 is supplied to the heat exchanger 9 through a chilled water feed line 112 by a water pump 111, and the water after passing through the heat exchanger 9 flows through a chilled water return line 113. Returned to cooling tower 110 . By cooling the treated water by heat exchange with cold water as a cooling fluid in the heat exchanger 9, the temperature in the treatment tank 3 can be lowered and the object 2 to be treated can be cooled.

冷水送り路112には冷水送り弁114が設けられ、冷水戻し路113には冷水戻し弁115が設けられている。冷水送り弁114及び冷水戻し弁115を開いた状態で送水ポンプ111を作動させると、クーリングタワー110と熱交換器9の一次側との間で冷却水を循環させることができる。一方、冷水送り弁114及び冷水戻し弁115を閉じると、熱交換器9への冷水の通水を停止することができる。 A cold water feed valve 114 is provided in the cold water feed path 112 , and a cold water return valve 115 is provided in the cold water return path 113 . When the water pump 111 is operated with the cold water feed valve 114 and the cold water return valve 115 open, cooling water can be circulated between the cooling tower 110 and the primary side of the heat exchanger 9 . On the other hand, when the cold water feed valve 114 and the cold water return valve 115 are closed, the flow of cold water to the heat exchanger 9 can be stopped.

ドレン排出手段13は、給蒸手段10により熱交換器9に供給された加熱蒸気の凝縮水を外部へ排出する。ドレン排出手段13は、冷水戻し路113から分岐するドレン排出路130に、ドレン排出弁131、スチームトラップ132、及び逆止弁133が順に設けられて構成される。熱交換器9への蒸気供給時、ドレン排出弁131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 13 discharges the condensed water of the heating steam supplied to the heat exchanger 9 by the steam supply means 10 to the outside. The drain discharge means 13 includes a drain discharge valve 131 , a steam trap 132 , and a check valve 133 provided in this order in a drain discharge path 130 branched from the cold water return path 113 . By opening the drain discharge valve 131 when supplying steam to the heat exchanger 9, the condensed water of the steam can drop downward and be discharged to the outside.

異常検出手段16は、熱交換器9における処理水又は冷却用流体としての冷水の熱交換前後の状態量変化に基づき、熱交換器9における処理水の冷却の異常を検出する。熱交換器9における処理水の冷却異常の要因は、クーリングタワー110本体の異常(例えば、送風機の故障)、冷水の循環における異常(例えば、クーリングタワー110における渇水、送水ポンプ111へのエア噛み、冷水送り路112又は冷水戻し路113の閉塞)、熱交換器9の異常(例えば、熱交換器9内の管路の閉塞)、処理水の循環における異常(例えば、循環ポンプ81へのエア噛み、循環路80の閉塞)等多岐にわたる。このうち、冷水及び処理水の循環における異常、及び熱交換器9の異常に起因する冷却異常については、熱交換前の状態量のみ又は熱交換後の状態量のみを監視対象とした場合に検出が困難なものが存在する。例えば、冷水送り路112中の熱交換前の冷水の温度又は圧力のみを監視対象とした場合、下流側における熱交換器9の管路や冷水戻し路113の閉塞に起因する冷却異常の検出が困難となる。本発明においては、処理水又は冷水の熱交換前及び熱交換後の2点間における状態量変化を監視することで、熱交換前後いずれかの状態量のみを監視対象とした場合には検出が困難な冷却異常を検出可能とする。 The abnormality detection means 16 detects an abnormality in the cooling of the treated water in the heat exchanger 9 based on the state quantity change before and after the heat exchange of the treated water or the cold water as the cooling fluid in the heat exchanger 9 . Causes of abnormal cooling of the treated water in the heat exchanger 9 include an abnormality in the cooling tower 110 (for example, failure of the blower), an abnormality in cold water circulation (for example, water shortage in the cooling tower 110, air entrainment in the water pump 111, cold water supply line 112 or cold water return line 113), abnormality in the heat exchanger 9 (e.g., clogging of the pipeline in the heat exchanger 9), abnormality in circulation of treated water (e.g., air entrapment in the circulation pump 81, circulation blockage of the path 80). Of these, abnormalities in the circulation of cold water and treated water, and cooling abnormalities caused by abnormalities in the heat exchanger 9 are detected when only the state quantity before heat exchange or only the state quantity after heat exchange is monitored. is difficult. For example, if only the temperature or pressure of the chilled water before heat exchange in the chilled water feed path 112 is monitored, a cooling abnormality caused by clogging of the pipe line of the heat exchanger 9 or the chilled water return path 113 on the downstream side may not be detected. becomes difficult. In the present invention, by monitoring the state quantity change between two points before and after heat exchange of treated water or cold water, detection is not possible when only one of the state quantities before and after heat exchange is monitored. Enable detection of difficult cooling anomalies.

本実施形態においては、状態量として圧力に着目し、主冷却手段11から供給される冷水の熱交換前後の圧力差ΔPに基づき異常を検出する。本実施形態の異常検出手段16は、差圧スイッチ16aを備える。差圧スイッチ16aは、高圧側接続口16bが熱交換器9の一次側の入口付近に、低圧側接続口16cが熱交換器9の一次側の出口付近に接続されている。本実施形態の差圧スイッチ16aの高圧側接続口16bは、冷水送り路112に接続されており、冷水送り路112における冷水送り弁114よりも下流側(熱交換器9側)且つ給蒸路100と冷水送り路112の合流部よりも上流側(クーリングタワー110側)に接続されている。また、低圧側接続口16cは、冷水戻し路113に接続されており、冷水戻し路113における冷水戻し弁115、及び冷水戻し路113とドレン排出路130の分岐部よりも上流側(熱交換器9側)に接続されている。 In this embodiment, attention is focused on pressure as a state quantity, and an abnormality is detected based on the pressure difference ΔP before and after heat exchange of cold water supplied from the main cooling means 11 . The abnormality detection means 16 of this embodiment includes a differential pressure switch 16a. The differential pressure switch 16 a has a high pressure side connection port 16 b connected near the primary side inlet of the heat exchanger 9 and a low pressure side connection port 16 c connected near the primary side outlet of the heat exchanger 9 . The high-pressure side connection port 16b of the differential pressure switch 16a of the present embodiment is connected to the cold water feed path 112, and is downstream of the cold water feed valve 114 in the cold water feed path 112 (the side of the heat exchanger 9) and the steam supply path. 100 and the cold water feed path 112 are connected to the upstream side (cooling tower 110 side). In addition, the low-pressure side connection port 16c is connected to the cold water return path 113, and upstream of the cold water return valve 115 in the cold water return path 113 and the branch portion of the cold water return path 113 and the drain discharge path 130 (heat exchanger 9 side).

熱交換器9の一次側及び二次側において、冷水及び処理水の圧力は、それぞれ上流から下流へ向かって降下する。このような圧力損失は、内部の管路の形状が複雑である熱交換器9において特に顕著であり、また流体の流速が大きいほど大きくなる。従って、クーリングタワー110から冷水が十分な量正常に供給されている状態では、熱交換前後における冷水の圧力差は比較的大きくなる。一方、クーリングタワー110における渇水や送水ポンプ111へのエア噛み、冷水が流通する管路の閉塞等の異常により、クーリングタワー110からの冷水の供給量が不足したり、クーリングタワー110と熱交換器9との間で冷水の循環が滞ると、熱交換前後における冷水の圧力差ΔPが低下する。本実施形態の差圧スイッチ16aは、冷水送り路112を熱交換器9に向かって通過する冷水と、処理水との熱交換後に冷水戻し路113を通過する水との圧力差ΔPを検知し、圧力差ΔPが所定値TH以下となった場合に制御手段15に対して警報信号を出力する。 On the primary and secondary sides of the heat exchanger 9, the cold water and treated water pressures respectively drop from upstream to downstream. Such a pressure loss is particularly conspicuous in the heat exchanger 9 in which the shape of the internal pipes is complicated, and increases as the flow velocity of the fluid increases. Therefore, in a state in which a sufficient amount of cold water is normally supplied from the cooling tower 110, the pressure difference of the cold water before and after heat exchange is relatively large. On the other hand, due to an abnormality such as water shortage in the cooling tower 110, air entrapment in the water pump 111, or clogging of the pipe line through which cold water flows, the amount of cold water supplied from the cooling tower 110 is insufficient, or the cooling tower 110 and the heat exchanger 9 do not function properly. If the circulation of cold water is stagnant between them, the pressure difference ΔP of the cold water before and after heat exchange is reduced. The differential pressure switch 16a of this embodiment detects the pressure difference ΔP between the cold water passing through the cold water feed path 112 toward the heat exchanger 9 and the water passing through the cold water return path 113 after heat exchange with the treated water. , and outputs an alarm signal to the control means 15 when the pressure difference ΔP becomes equal to or less than a predetermined value THP .

制御手段15は、温度センサや水位検出器の検出信号、異常検出手段16からの警報信号、経過時間などに基づき、上述した各手段を制御する。制御手段15は、具体的には、給水ポンプ41、給水弁42、排水弁51、加圧弁61、排気弁71、循環ポンプ81、給蒸弁101、送水ポンプ111、冷水送り弁114、冷水戻し弁115、ドレン排出弁131等を制御する。また、制御手段15には、温度センサ、水位検出器、及び異常検出手段16などが接続されている。制御手段15は、後述するように、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。 The control means 15 controls each means described above based on detection signals from the temperature sensor and the water level detector, alarm signals from the abnormality detection means 16, elapsed time, and the like. Specifically, the control means 15 includes a water supply pump 41, a water supply valve 42, a water discharge valve 51, a pressurization valve 61, an exhaust valve 71, a circulation pump 81, a steam supply valve 101, a water supply pump 111, a cold water feed valve 114, and a cold water return. It controls the valve 115, the drain discharge valve 131, and the like. A temperature sensor, a water level detector, an abnormality detection means 16 and the like are connected to the control means 15 . As will be described later, the control means 15 performs heat sterilization and subsequent cooling of the objects 2 to be treated in the treatment bath 3 according to a predetermined procedure (program).

なお、上記構成の制御手段15は、具体的には例えば、CPU、メモリ(例えばフラッシュメモリ)、入力部及び出力部を備えた情報処理装置により構成することができる。そして、情報処理装置により構成された制御手段15の上述した各構成要素による処理は、メモリに記憶されたプログラムをCPUが読み出して実行することで行われる。情報処理装置としては、例えば、パーソナルコンピュータ、PLC(プログラマラブルロジックコントローラ)あるいはマイコンが用いられる。ただし、制御手段15の一部の機能を、任意の通信手段により接続されたクラウド上で実行されるよう構成しても良い。 It should be noted that the control means 15 configured as described above can be specifically configured by an information processing device having a CPU, a memory (for example, a flash memory), an input section, and an output section. Then, the processing by each component of the control means 15 configured by the information processing device is performed by the CPU reading and executing the program stored in the memory. For example, a personal computer, a PLC (Programmable Logic Controller), or a microcomputer is used as the information processing device. However, some functions of the control means 15 may be configured to be executed on a cloud connected by any communication means.

2.殺菌装置1の動作
制御手段15は、所定の手順(プログラム)に従い、各種の弁及びポンプを制御することによって処理槽3内の被処理物2の加熱殺菌やその後の冷却を行う。具体的には、図2に示すように、制御手段15は、処理槽3内に被処理物2を収容した状態で、処理槽3内への給水工程S1、殺菌工程S3へ移行するための移行工程S2、被処理物2を加熱殺菌する殺菌工程S3、主冷却手段11により加熱殺菌後の被処理物2を冷却する主冷却工程S4、処理槽3内からの排水工程S7を順次実行する。また、主冷却工程S4と並行して、熱交換器9における処理水の冷却の異常を検出する異常検出工程S5を実行し、異常検出工程S5において異常が検出された場合には補助冷却工程S6が実行される。以下、各工程をより詳細に説明する。
2. Operation of the sterilizer 1 The control means 15 controls various valves and pumps according to a predetermined procedure (program) to perform heat sterilization and subsequent cooling of the object 2 in the treatment tank 3 . Specifically, as shown in FIG. 2, the control means 15 controls the water supply step S1 into the treatment tank 3 and the sterilization step S3 in a state in which the object 2 is stored in the treatment tank 3. A transfer step S2, a sterilization step S3 for heating and sterilizing the object 2 to be treated, a main cooling step S4 for cooling the object 2 after heat sterilization by the main cooling means 11, and a step S7 for discharging water from the treatment tank 3 are sequentially executed. . Further, in parallel with the main cooling step S4, an abnormality detection step S5 for detecting an abnormality in the cooling of the treated water in the heat exchanger 9 is performed, and when an abnormality is detected in the abnormality detection step S5, the auxiliary cooling step S6 is executed. Each step will be described in more detail below.

<給水工程S1>
給水工程S1では、制御手段15は、給水手段4により処理槽3内に給水を行い、処理槽3内に設定水位まで水を貯留する。具体的には、給水手段4は、給水ポンプ41を作動させた状態で給水弁42を開くことで給水を行う。処理槽3内に設定水位まで水が貯留されたことは、水位検出器により検出できる。
<Water supply step S1>
In the water supply step S1, the control means 15 causes the water supply means 4 to supply water into the processing tank 3, and the water is stored in the processing tank 3 up to a set water level. Specifically, the water supply unit 4 supplies water by opening the water supply valve 42 while the water supply pump 41 is in operation. A water level detector can detect that water has been stored in the treatment tank 3 up to the set water level.

設定水位として、処理槽3内のいずれの被処理物2も水没させない水位を設定可能であり、好ましくはさらに低い水位として、処理槽3内のいずれの被処理物2も浸漬しない水位が設定される。また、熱交換器9における処理水の冷却の異常が発生した場合に追加の給水を行えるよう、処理槽3内のいずれの被処理物2も浸漬しない最大水位よりも低い水位を設定水位として設定することがより好ましい。 As the set water level, it is possible to set a water level at which none of the objects 2 to be treated in the treatment tank 3 are submerged. be. In addition, a water level lower than the maximum water level at which none of the objects 2 to be treated in the treatment tank 3 is immersed is set as the set water level so that additional water can be supplied when an abnormality occurs in the cooling of the treated water in the heat exchanger 9. is more preferable.

<移行工程S2>
移行工程S2では、制御手段15は、循環手段8の循環ポンプ81を駆動させ、処理槽3と熱交換器9との間で処理水を循環させながら、その処理水を熱交換器9において給蒸手段10により加熱して、処理槽3内の温度を上昇させる。具体的には、制御手段15は、給蒸弁101を開くことで熱交換器9に加熱蒸気を供給して、処理水を加熱する。また、移行工程S2において、制御手段15は、ドレン排出手段13のドレン排出弁131を開けておき、蒸気の凝縮水を外部へ排出するようにしている。一方、移行工程S2において、制御手段15は、主冷却手段11の冷水送り弁114及び冷水戻し弁115を閉じておく。移行工程S2の開始から所定の移行時間が経過するか、処理槽3内が殺菌温度まで上昇すると、移行工程S2を終了する。
<Transition step S2>
In the transition step S2, the control means 15 drives the circulation pump 81 of the circulation means 8 to circulate the treated water between the treatment tank 3 and the heat exchanger 9, while supplying the treated water to the heat exchanger 9. The temperature in the processing tank 3 is raised by heating with the steaming means 10 . Specifically, the control means 15 supplies heating steam to the heat exchanger 9 by opening the steam supply valve 101 to heat the treated water. Further, in the transition step S2, the control means 15 opens the drain discharge valve 131 of the drain discharge means 13 to discharge the condensed water of the steam to the outside. On the other hand, in the transition step S2, the control means 15 keeps the cold water feed valve 114 and the cold water return valve 115 of the main cooling means 11 closed. When a predetermined transition time elapses from the start of the transition step S2, or when the inside of the treatment tank 3 rises to the sterilization temperature, the transition step S2 is terminated.

移行工程S2の開始以降、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)が破裂するのを防止するために、加圧手段6の加圧弁61と排気手段7の排気弁71とを制御して、処理槽3内の温度に応じた加圧がなされる。以後、循環手段8による水の循環と、処理槽3内の加圧とは、主冷却工程S4及び補助冷却工程S6の終了まで引き続きなされる。 After the start of the transition step S2, the pressure valve 61 of the pressure means 6 and the exhaust valve 71 of the exhaust means 7 are installed in order to prevent the material to be processed 2 from expanding due to heating and the package (such as a retort pouch) from bursting. is controlled to pressurize according to the temperature in the processing tank 3 . Thereafter, circulation of water by the circulation means 8 and pressurization in the processing tank 3 are continued until the main cooling step S4 and the sub-cooling step S6 are completed.

<殺菌工程S3>
殺菌工程S3では、制御手段15は、循環手段8により処理槽3と熱交換器9との間で水を循環させながら給蒸手段10による熱交換器9への蒸気供給を制御することで処理水を加熱して殺菌水とし、これにより処理槽3内を殺菌温度に維持して処理槽3内の被処理物2を加熱して殺菌する。具体的には、制御手段15は、給蒸弁101の開度を調整することで、処理槽3の温度センサの検出温度を殺菌温度以上に維持する。また、殺菌工程S3においても、制御手段15は、ドレン排出手段13のドレン排出弁131を開けておき、蒸気の凝縮水を外部へ排出するようにしている。一方、殺菌工程S3において、制御手段15は、主冷却手段11の冷水送り弁114及び冷水戻し弁115を閉じておく。
<Sterilization step S3>
In the sterilization step S3, the control means 15 controls the supply of steam to the heat exchanger 9 by the steam supply means 10 while circulating water between the treatment tank 3 and the heat exchanger 9 by the circulation means 8. Water is heated to make sterilizing water, and the inside of the processing tank 3 is thereby maintained at the sterilization temperature, and the object 2 to be processed in the processing tank 3 is heated and sterilized. Specifically, the control means 15 adjusts the opening degree of the steam supply valve 101 to maintain the temperature detected by the temperature sensor of the treatment bath 3 at or above the sterilization temperature. Also in the sterilization step S3, the control means 15 opens the drain discharge valve 131 of the drain discharge means 13 to discharge the condensed water of the steam to the outside. On the other hand, in the sterilization step S3, the control means 15 keeps the cold water feed valve 114 and the cold water return valve 115 of the main cooling means 11 closed.

処理槽3内が殺菌温度以上の状態で所定の殺菌時間が経過すると、制御手段15は、給蒸手段10による熱交換器9への蒸気供給を停止して、殺菌工程S3を終了する。具体的には、制御手段15は、給蒸手段10の給蒸弁101を閉じる。なお、前述したように、殺菌工程S3では、加圧手段6と排気手段7とを制御して、処理槽3内を、大気圧を超える設定圧力(処理槽3内温度相当の飽和蒸気圧力よりもやや高圧)に維持される。 When a predetermined sterilization time elapses while the inside of the treatment bath 3 is at the sterilization temperature or higher, the control means 15 stops the supply of steam to the heat exchanger 9 by the steam supply means 10, and terminates the sterilization step S3. Specifically, the control means 15 closes the steam supply valve 101 of the steam supply means 10 . As described above, in the sterilization step S3, the pressurizing means 6 and the exhausting means 7 are controlled to set the inside of the processing tank 3 to a set pressure exceeding the atmospheric pressure (more than the saturated steam pressure corresponding to the temperature inside the processing tank 3). maintained at a slightly higher pressure).

<主冷却工程S4>
主冷却工程S4では、制御手段15は、循環手段8により処理槽3と熱交換器9との間で水を循環させながら主冷却手段11により熱交換器9に冷却用流体としての冷水を供給することで処理水を冷却し、これにより処理槽3内の被処理物2を冷却する。具体的には、制御手段15は、主冷却手段11の冷水送り弁114及び冷水戻し弁115を開くとともに送水ポンプ111を駆動し、ドレン排出手段13のドレン排出弁131を閉じることで、クーリングタワー110と熱交換器9の間で冷水を循環させる。なお、主冷却工程S4において、制御手段15は、給蒸手段10の給蒸弁101を閉じておく。
<Main cooling step S4>
In the main cooling step S4, the control means 15 supplies cold water as a cooling fluid to the heat exchanger 9 by the main cooling means 11 while circulating water between the treatment tank 3 and the heat exchanger 9 by means of the circulation means 8. This cools the treated water, thereby cooling the object 2 in the treatment tank 3 . Specifically, the control means 15 opens the cold water feed valve 114 and the cold water return valve 115 of the main cooling means 11 , drives the water feed pump 111 , and closes the drain discharge valve 131 of the drain discharge means 13 so that the cooling tower 110 and the heat exchanger 9 to circulate cold water. In addition, in the main cooling step S4, the control means 15 keeps the steam supply valve 101 of the steam supply means 10 closed.

主冷却工程S4の開始から所定の冷却時間が経過するか、又は処理槽3内の温度が予め設定された冷却温度まで下がると、制御手段15は、冷水送り弁114及び冷水戻し弁115を閉じるとともに送水ポンプ111を停止させる。これにより、主冷却手段11による熱交換器9への冷水の供給を停止して、主冷却工程S4を終了する。 When a predetermined cooling time elapses from the start of the main cooling step S4, or when the temperature in the processing tank 3 drops to a preset cooling temperature, the control means 15 closes the cold water feed valve 114 and the cold water return valve 115. At the same time, the water pump 111 is stopped. As a result, the supply of cold water to the heat exchanger 9 by the main cooling means 11 is stopped, and the main cooling step S4 ends.

<異常検出工程S5>
主冷却工程S4が開始されると、並行して異常検出工程S5が実行される。異常検出工程S5では、制御手段15は、異常検出手段16により主冷却手段11から供給される冷水の熱交換前後の圧力差ΔPを監視し、所定の条件に従って異常を検出する。具体的には、制御手段15は、差圧スイッチ16aにより冷水送り路112通過する冷水と冷水戻し路113を通過する水との圧力差ΔPを検知し、当該圧力差ΔPが所定値TH以下となり差圧スイッチ16aからの警報信号を受け取った場合に、処理水の冷却に異常が発生したと判定する。異常判定における所定値THは、クーリングタワー110から送られる冷水の流量、冷水送り路112及び冷水戻し路113の管路の長さ及び内径、熱交換器9の構造、異常検出手段16の構造(例えば、高圧側接続口16bと低圧側接続口16cの間の高低差(鉛直方向における距離))等を考慮して、適宜設定される。
<Abnormality detection step S5>
When the main cooling process S4 is started, the abnormality detection process S5 is executed in parallel. In the abnormality detection step S5, the control means 15 monitors the pressure difference ΔP before and after the heat exchange of cold water supplied from the main cooling means 11 by the abnormality detection means 16, and detects abnormality according to predetermined conditions. Specifically, the control means 15 detects the pressure difference ΔP between the cold water passing through the cold water supply path 112 and the water passing through the cold water return path 113 by the differential pressure switch 16a, and the pressure difference ΔP is equal to or less than a predetermined value TH P. When an alarm signal is received from the differential pressure switch 16a, it is determined that an abnormality has occurred in the cooling of the treated water. The predetermined value THP in the abnormality determination is the flow rate of cold water sent from the cooling tower 110, the length and inner diameter of the cold water supply path 112 and the cold water return path 113, the structure of the heat exchanger 9, the structure of the abnormality detection means 16 ( For example, the height difference (the distance in the vertical direction) between the high-voltage side connection port 16b and the low-voltage side connection port 16c is taken into account, and the distance is appropriately set.

<補助冷却工程S6>
処理水の冷却の異常が発生したと判定されると、補助冷却工程S6が開始される。補助冷却工程S6では、制御手段15は、補助冷却手段としての給水手段4により処理槽3内へ追加で比較的低温の水を供給し、循環手段8により当該水を循環路80に流通させることにより、処理槽3内の被処理物2を冷却する。給水手段4は、給水工程S1における運転と同様に、給水ポンプ41を作動させた状態で給水弁42を開くことで給水を行う。
<Auxiliary cooling step S6>
If it is determined that the cooling abnormality of the treated water has occurred, the auxiliary cooling step S6 is started. In the auxiliary cooling step S6, the control means 15 additionally supplies relatively low-temperature water into the processing tank 3 by the water supply means 4 as the auxiliary cooling means, and circulates the water through the circulation path 80 by the circulation means 8. cools the object to be processed 2 in the processing tank 3 . The water supply means 4 supplies water by opening the water supply valve 42 while the water supply pump 41 is in operation, as in the operation in the water supply step S1.

また、追加の給水及び水の循環と並行して、制御手段15は、排水手段5により処理水の一部を排水する。具体的には、制御手段15は、排水弁51を開いて処理槽3内の処理水の一部を外部へ排出する。これにより、被処理物2の冷却を効率的に行うととともに、追加の給水により処理層内の被処理物2が水中に浸漬することを回避できる。 In parallel with the additional water supply and water circulation, the control means 15 causes the drainage means 5 to drain part of the treated water. Specifically, the control means 15 opens the drain valve 51 and discharges part of the treated water in the treatment tank 3 to the outside. As a result, it is possible to efficiently cool the object 2 to be treated and prevent the object 2 to be treated in the treatment layer from being immersed in water due to additional water supply.

なお、補助冷却工程S6において、給水手段4による追加の給水、及び排水手段5による処理水の排水は、連続的に行っても、間欠に行ってもよく、追加の給水と処理水の排水とを交互に行っても良い。また、排水時の循環ポンプ81へのエア噛みを防止するために、補助冷却工程S6において、追加の給水と、循環手段8による水の循環と、処理水の排水とを、この順に繰り返してもよい。 In the auxiliary cooling step S6, the additional water supply by the water supply means 4 and the drainage of the treated water by the drainage means 5 may be performed continuously or intermittently. may be performed alternately. Further, in order to prevent air from entering the circulation pump 81 during drainage, additional water supply, circulation of water by the circulation means 8, and drainage of treated water may be repeated in this order in the auxiliary cooling step S6. good.

なお、補助冷却工程S6の開始後は、主冷却手段11から熱交換器9への冷水の供給を停止して主冷却工程S4を終了又は一時停止してもよい。例えば、主冷却手段11の異常への対応のためにクーリングタワー110の動作を一次停止し、補助冷却手段のみで冷却を行ってもよい。或いは、主冷却手段11から熱交換器9への冷水の供給を続けて主冷却工程S4を続行してもよい。例えば、圧力差ΔPの低下量が比較的小さく、主冷却手段11により不十分ではあるがいくらかの冷却効果が見込める場合には、主冷却手段11及び補助冷却手段の両方により冷却を行っても良い。 After starting the auxiliary cooling step S6, the supply of cold water from the main cooling means 11 to the heat exchanger 9 may be stopped to end or temporarily stop the main cooling step S4. For example, the operation of the cooling tower 110 may be temporarily stopped in order to deal with an abnormality of the main cooling means 11, and cooling may be performed only by the auxiliary cooling means. Alternatively, the supply of cold water from the main cooling means 11 to the heat exchanger 9 may be continued to continue the main cooling step S4. For example, if the amount of decrease in the pressure difference ΔP is relatively small and some cooling effect, though insufficient, can be expected from the main cooling means 11, cooling may be performed by both the main cooling means 11 and the auxiliary cooling means. .

補助冷却工程S6の開始から所定の時間が経過するか、又は処理槽3内の温度が予め設定された冷却温度まで下がると、制御手段15は、給水弁42を閉じるとともに給水ポンプ41を停止させる。これにより、給水手段4による処理槽3への給水を停止して補助冷却工程S6を終了する。或いは、補助冷却工程S6の実行中に異常検出手段16による圧力差ΔPの監視を継続し、主冷却手段11の異常への対応によりクーリングタワー110と熱交換器9との間で冷水の正常な循環が再開し圧力差ΔPが所定値THを上回った時点で、補助冷却工程S6を終了し、主冷却工程S4を再開してもよい。 When a predetermined time elapses from the start of the auxiliary cooling step S6, or when the temperature in the processing tank 3 drops to a preset cooling temperature, the control means 15 closes the water supply valve 42 and stops the water supply pump 41. . As a result, the water supply to the processing tank 3 by the water supply means 4 is stopped, and the sub-cooling step S6 is completed. Alternatively, the abnormality detection means 16 continues to monitor the pressure difference ΔP during the execution of the auxiliary cooling step S6, and the normal circulation of cold water between the cooling tower 110 and the heat exchanger 9 is achieved by coping with the abnormality of the main cooling means 11. is resumed and the pressure difference ΔP exceeds a predetermined value THP , the sub-cooling step S6 may be terminated and the main cooling step S4 resumed.

<排水工程S7>
排水工程S7では、排水手段5により処理槽3内から処理水を排水する。この際、制御手段15は、加圧弁61を開いて加圧手段6により処理槽3内を加圧した状態で排水弁51を開くことで、処理槽3内から外部へ水を迅速に排出できる。その後、加圧弁61を閉じる一方、排気手段7の排気弁71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。
<Drainage process S7>
In the drainage step S7, the treated water is drained from the treatment tank 3 by the drainage means 5. As shown in FIG. At this time, the control means 15 opens the water discharge valve 51 in a state in which the pressurizing valve 61 is opened and the inside of the processing tank 3 is pressurized by the pressurizing means 6, so that the water can be quickly discharged from the processing tank 3 to the outside. . After that, the pressure valve 61 is closed and the exhaust valve 71 of the exhaust means 7 is opened to return the inside of the processing tank 3 to atmospheric pressure. can be taken out.

3.作用効果
本実施形態の殺菌装置1は、異常検出手段16を備える。制御手段15は、主冷却工程S4と並行して異常検出手段16により処理水又は冷却用流体としての冷水の熱交換前後の状態量変化を監視する。これにより、熱交換器9における処理水の冷却状態を監視し、異常が発生した場合に早期に適切な対応を行って被処理物2の過加熱を回避することが可能となる。
3. Effect The sterilizer 1 of this embodiment includes an abnormality detection means 16 . In parallel with the main cooling step S4, the control means 15 monitors the state quantity change before and after the heat exchange of cold water as treated water or cooling fluid by the abnormality detection means 16 . As a result, it is possible to monitor the cooling state of the treated water in the heat exchanger 9 and to take appropriate measures early in the event of an abnormality, thereby avoiding overheating of the object 2 to be treated.

本実施形態の異常検出手段16は、差圧スイッチ16aを備え、主冷却手段11から供給される冷水の熱交換前後の圧力差ΔPを検知する。熱交換器9の一次側における入口及び出口付近における冷水の圧力差ΔPが検知されるため、クーリングタワー110における渇水や送水ポンプ111へのエア噛み、冷水が流通する管路の閉塞等の、冷水の循環における異常を要因とする種々の異常を検出可能である。 The abnormality detection means 16 of this embodiment includes a differential pressure switch 16a and detects a pressure difference ΔP between before and after heat exchange of cold water supplied from the main cooling means 11 . Since the cold water pressure difference ΔP near the inlet and the outlet on the primary side of the heat exchanger 9 is detected, it is possible to detect cold water problems such as drought in the cooling tower 110, air entrapment in the water pump 111, blockage of the pipe line through which cold water flows, and the like. A variety of abnormalities can be detected due to abnormalities in circulation.

また、本実施形態の殺菌装置1の給水手段4は、補助冷却手段としての機能を有する。これにより、処理水の冷却に異常が発生した場合、給水手段4により処理槽3内へ追加で比較的低温の水を供給することで、処理槽3内の被処理物2を冷却でき、被処理物2の過加熱を回避することが可能となる。また、殺菌装置1が元来備える給水手段4を補助冷却手段として利用することで、冷却異常時の補助冷却のために新たな装置を導入する必要がない。 Moreover, the water supply means 4 of the sterilization apparatus 1 of this embodiment has a function as an auxiliary cooling means. As a result, when an abnormality occurs in the cooling of the treated water, relatively low-temperature water is additionally supplied into the treatment tank 3 by the water supply means 4, whereby the object 2 to be treated in the treatment tank 3 can be cooled. It becomes possible to avoid overheating of the workpiece 2 . Further, by using the water supply means 4 originally provided in the sterilization apparatus 1 as auxiliary cooling means, there is no need to introduce a new device for auxiliary cooling in the event of a cooling abnormality.

4.他の実施形態
なお、本発明は、以下の態様でも実施可能である。
4. Other Embodiments The present invention can also be implemented in the following aspects.

上記実施形態では、異常検出手段16が冷水の熱交換前後の圧力差ΔPに基づき異常を検出したが、異常検出手段16の構成はこれに限定されるものではない。一例として、状態量として温度に着目し、異常検出手段16を、熱交換器9における処理水の熱交換前後の温度差ΔT1に基づき異常を検出するように構成してもよい。この場合、異常検出手段16は2台の温度センサを備える。一方の温度センサは、熱交換器9の二次側の入口付近(例えば、循環路80における循環ポンプ81と熱交換器9との間の位置)に設けられ、処理槽3から熱交換器9へ向かって循環路80を通過する処理水の温度T1inを検出する。他方の温度センサは、熱交換器9の二次側の出口付近(例えば、熱交換器9から処理槽3へ向かう循環路80の中途)に設けられ、冷水との熱交換後に熱交換器9から処理槽3へ向かって循環路80を通過する処理水の温度T1outを検出する。そして、制御手段15において、温度差ΔT1=T1in-T1outを算出し、温度差ΔT1が所定値THT1以下となった場合に、処理水の冷却に異常が発生したと判定する。 In the above embodiment, the abnormality detection means 16 detects an abnormality based on the pressure difference ΔP before and after heat exchange of cold water, but the configuration of the abnormality detection means 16 is not limited to this. As an example, focusing on temperature as a state quantity, the abnormality detection means 16 may be configured to detect an abnormality based on the temperature difference ΔT1 before and after heat exchange of the treated water in the heat exchanger 9 . In this case, the abnormality detection means 16 has two temperature sensors. One temperature sensor is provided near the inlet on the secondary side of the heat exchanger 9 (for example, a position between the circulation pump 81 and the heat exchanger 9 in the circulation path 80). A temperature T1 in of the treated water passing through the circulation path 80 toward is detected. The other temperature sensor is provided near the outlet on the secondary side of the heat exchanger 9 (for example, in the middle of the circulation path 80 from the heat exchanger 9 to the treatment tank 3), and after heat exchange with cold water, the heat exchanger 9 , the temperature T1 out of the treated water passing through the circulation path 80 toward the treatment tank 3 is detected. Then, the temperature difference ΔT1=T1 in −T1 out is calculated by the control means 15, and when the temperature difference ΔT1 becomes equal to or less than a predetermined value TH T1 , it is determined that an abnormality has occurred in the cooling of the treated water.

別の例として、状態量として温度に着目し、異常検出手段16を、熱交換器9における冷却用流体としての冷水の熱交換前後の温度差ΔT2に基づき異常を検出するように構成してもよい。この場合、異常検出手段16は2台の温度センサを備える。一方の温度センサは、熱交換器9の一次側の入口付近(例えば、冷水送り路112における冷水送り弁114よりも下流側)に設けられ、クーリングタワー110から熱交換器9へ向かって冷水送り路112を通過する冷水の温度T2inを検出する。他方の温度センサは、熱交換器9の一次側の出口付近(例えば、冷水戻し路113における冷水戻し弁115よりも上流側)に設けられ、処理水との熱交換後に熱交換器9からクーリングタワー110へ向かって冷水戻し路113を通過する水の温度T2outを検出する。そして、制御手段15において、温度差ΔT2=T2out-T2inを算出し、温度差ΔT2が所定値THT2以下となった場合に、処理水の冷却に異常が発生したと判定する。このように、異常検出手段16を、処理水又は冷水の熱交換前後の温度差に基づき熱交換器9における冷却の異常を検出するよう構成することによっても、熱交換器9における処理水の冷却状態を監視することができる。 As another example, focusing on the temperature as the state quantity, the abnormality detection means 16 may be configured to detect an abnormality based on the temperature difference ΔT2 before and after the heat exchange of cold water as the cooling fluid in the heat exchanger 9. good. In this case, the abnormality detection means 16 has two temperature sensors. One temperature sensor is provided near the inlet on the primary side of the heat exchanger 9 (for example, downstream of the cold water feed valve 114 in the cold water feed passage 112), The temperature T2 in of the chilled water passing through 112 is detected. The other temperature sensor is provided near the outlet on the primary side of the heat exchanger 9 (for example, upstream of the chilled water return valve 115 in the chilled water return path 113), and after heat exchange with the treated water, the temperature sensor is discharged from the heat exchanger 9 to the cooling tower. The temperature T2 out of the water passing through the cold water return path 113 towards 110 is detected. Then, the temperature difference ΔT2=T2 out −T2 in is calculated by the control means 15, and when the temperature difference ΔT2 becomes equal to or less than a predetermined value TH T2 , it is determined that an abnormality has occurred in the cooling of the treated water. In this way, by configuring the abnormality detection means 16 to detect a cooling abnormality in the heat exchanger 9 based on the temperature difference between before and after the heat exchange of the treated water or cold water, cooling of the treated water in the heat exchanger 9 status can be monitored.

なお、異常の判定に用いられる所定値THT1,THT2は、主冷却工程S4の開始後の経過時間に応じて変化するように設定してもよい。通常、処理水又は冷水の熱交換前後の温度差は、冷却の開始後直後は比較的大きく、その後冷却の進行とともに徐々に小さくなる。従って、所定値THT1,THT2を、主冷却工程S4の開始後の経過時間に応じて連続的又は段階的に小さくなるように設定してもよい。 It should be noted that the predetermined values TH T1 and TH T2 used for determining abnormality may be set so as to change according to the elapsed time after the start of the main cooling step S4. Normally, the temperature difference between treated water or cold water before and after heat exchange is relatively large immediately after the start of cooling, and then gradually decreases as cooling progresses. Therefore, the predetermined values TH T1 and TH T2 may be set to decrease continuously or stepwise according to the elapsed time after the start of the main cooling step S4.

さらに別の例として、異常検出手段16を、冷却用流体としての冷水の流量に基づき異常を検出するように構成してもよい。この場合、異常検出手段16は流量計を備える。当該流量計は、熱交換器9の一次側の入口付近(例えば、冷水送り路112における冷水送り弁114よりも下流側)に設けられ、クーリングタワー110から熱交換器9へ向かって冷水送り路112を通過する冷水の流量Vinを測定する。そして、制御手段15において、流量Vinが所定値TH以下となった場合に、処理水の冷却に異常が発生したと判定する。或いは、流量計を、熱交換器9の一次側の出口付近(例えば、冷水戻し路113における冷水戻し弁115よりも上流側)に設け、処理水との熱交換後に熱交換器9からクーリングタワー110へ向かって冷水戻し路113を通過する水の流量Voutを測定し、制御手段15において同様の判定を行ってもよい。
このように、異常検出手段16を、冷水の流量に基づき熱交換器9における冷却の異常を検出するよう構成することによっても、熱交換器9における処理水の冷却状態を監視することができる。
As still another example, the abnormality detection means 16 may be configured to detect an abnormality based on the flow rate of cold water as the cooling fluid. In this case, the abnormality detection means 16 comprises a flow meter. The flow meter is provided near the inlet on the primary side of the heat exchanger 9 (for example, downstream of the cold water feed valve 114 in the cold water feed path 112), and flows from the cooling tower 110 toward the heat exchanger 9. Measure the cold water flow rate V in through the . Then, in the control means 15, when the flow rate Vin becomes equal to or less than a predetermined value THV , it is determined that an abnormality has occurred in the cooling of the treated water. Alternatively, a flow meter is provided near the outlet on the primary side of the heat exchanger 9 (for example, upstream of the cold water return valve 115 in the cold water return path 113), and after heat exchange with the treated water, the heat exchanger 9 to the cooling tower 110 The flow rate V out of water passing through the cold water return path 113 toward the direction of the control means 15 may be measured and the similar determination may be made.
Thus, by configuring the abnormality detection means 16 to detect a cooling abnormality in the heat exchanger 9 based on the flow rate of cold water, the cooling state of the treated water in the heat exchanger 9 can be monitored.

また、上記実施形態では、補助冷却手段としての給水手段4が、補助冷却工程S6において処理槽3内へ追加で比較的低温の水を供給する構成としたが、給水手段4による給水先は、これに限定されるものではない。例えば、給水手段4から循環路80内に追加で給水する構成としてもよい。 In the above embodiment, the water supply means 4 as the auxiliary cooling means is configured to additionally supply relatively low-temperature water into the processing tank 3 in the auxiliary cooling step S6. It is not limited to this. For example, a configuration may be adopted in which water is additionally supplied from the water supply means 4 into the circulation path 80 .

また、上記実施形態では、主冷却手段11がクーリングタワー110を備える構成であるが、主冷却手段11がチラーを備える構成としてもよい。この場合も、チラーから熱交換器9に供給される冷水の状態量変化を監視することにより、処理水の冷却の異常を検出することが可能である。 Further, in the above embodiment, the main cooling means 11 is configured to include the cooling tower 110, but the main cooling means 11 may be configured to include a chiller. Also in this case, it is possible to detect an abnormality in the cooling of the treated water by monitoring changes in the state quantity of cold water supplied from the chiller to the heat exchanger 9 .

また、上記実施形態では、給水手段4を補助冷却手段として用いたが、補助冷却手段の構成はこれに限定されるものではなく、補助冷却手段として別途装置を導入してもよい。一例として、補助冷却手段としてチラーを導入してもよい。この場合、チラーは、熱交換器9の一次側に冷水(これを、第2冷却水と呼ぶ)を供給可能に構成される。主冷却工程S4では、主冷却手段11のクーリングタワー110から熱交換器9に冷水(これを、第1冷却水と呼ぶ)を供給することで処理水を冷却する。そして、処理水の冷却の異常が発生したと判定されると、補助冷却工程S6では、制御手段15は、チラーにより熱交換器9の一次側に第2冷却水を供給することにより、処理水を冷却する。なお、補助冷却手段として導入する装置はチラーに限定されず、クーリングタワーを補助冷却手段として導入し、殺菌装置1が主冷却手段11のクーリングタワー110と合わせて計2台のクーリングタワーを備える構成としてもよい。 Further, in the above embodiment, the water supply means 4 is used as the auxiliary cooling means, but the configuration of the auxiliary cooling means is not limited to this, and a separate device may be introduced as the auxiliary cooling means. As an example, a chiller may be introduced as an auxiliary cooling means. In this case, the chiller is configured to be able to supply cold water (this is called second cooling water) to the primary side of the heat exchanger 9 . In the main cooling step S4, the treated water is cooled by supplying cold water (referred to as first cooling water) from the cooling tower 110 of the main cooling means 11 to the heat exchanger 9 . Then, when it is determined that an abnormality has occurred in the cooling of the treated water, in the auxiliary cooling step S6, the control means 15 supplies the second cooling water to the primary side of the heat exchanger 9 by means of the chiller so that the treated water to cool. In addition, the device introduced as the auxiliary cooling means is not limited to the chiller, and a cooling tower may be introduced as the auxiliary cooling means, and the sterilization apparatus 1 may be configured to include a total of two cooling towers together with the cooling tower 110 of the main cooling means 11. .

別の例として、補助冷却手段として熱交換器9の一次側に水を供給する給水手段(これを、第1給水手段としての給水手段4に対して第2給水手段と呼ぶ)を導入してもよい。この場合、第2給水手段は、冷水送り弁114と熱交換器9の間の位置に接続された給水路を介して、給水源から冷水送り路112へ比較的低温の水を供給可能に構成される。当該給水路には、給水ポンプと給水弁とが設けられており、給水ポンプを作動させた状態で給水弁を開くことで冷水送り路112へ水を供給できる。第2給水手段から比較的低温の水を熱交換器9の一次側に供給することで、処理水を冷却する。また、第2給水手段を補助冷却手段として用いる場合、第2給水手段からの給水量に応じて排水を行う排水手段(これを、第1排水手段としての排水手段5に対して第2排水手段と呼ぶ)を設ける。第2排水手段は、冷水戻し路113においてドレン排出路130の分岐部と熱交換器9の間に位置に接続された排水路を介して、熱交換器9を通過後の水の少なくとも一部を外部へ排出する。 As another example, a water supply means for supplying water to the primary side of the heat exchanger 9 as an auxiliary cooling means (this is called a second water supply means in contrast to the water supply means 4 as the first water supply means) is introduced. good too. In this case, the second water supply means is configured to be able to supply relatively low-temperature water from the water supply source to the cold water supply path 112 via the water supply path connected between the cold water supply valve 114 and the heat exchanger 9. be done. A water supply pump and a water supply valve are provided in the water supply path, and water can be supplied to the cold water supply path 112 by opening the water supply valve while the water supply pump is in operation. By supplying relatively low temperature water to the primary side of the heat exchanger 9 from the second water supply means, the treated water is cooled. Further, when the second water supply means is used as the auxiliary cooling means, the water discharge means for discharging water according to the amount of water supplied from the second water supply means (this is the second water discharge means for the water discharge means 5 as the first water discharge means ) is provided. At least part of the water that has passed through the heat exchanger 9 through a drainage channel connected between the branch of the drain discharge channel 130 and the heat exchanger 9 in the cold water return channel 113 is discharged to the outside.

以上、本発明に係る種々の実施形態を説明したが、これらは例として提示したものであり、発明の範囲を限定することは意図していない。当該新規な実施形態は、その他の様々な形態で実施されることが可能であり、発明の要旨を逸脱しない範囲で、種々の省略、置き換え、変更を行うことができる。当該実施形態やその変形は、発明の範囲や要旨に含まれるとともに、特許請求の範囲に記載された発明とその均等の範囲に含まれる。 While various embodiments of the invention have been described above, they are presented by way of example and are not intended to limit the scope of the invention. The novel embodiment can be embodied in various other forms, and various omissions, replacements, and modifications can be made without departing from the scope of the invention. The embodiment and its modifications are included in the scope and gist of the invention, and are included in the scope of the invention described in the claims and its equivalents.

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 :循環手段
9 :熱交換器
10 :給蒸手段
11 :主冷却手段
13 :ドレン排出手段
15 :制御手段
16 :異常検出手段
16a :差圧スイッチ
16b :高圧側接続口
16c :低圧側接続口
20 :トレー
40 :給水路
41 :給水ポンプ
42 :給水弁
50 :排水路
51 :排水弁
52 :逆止弁
60 :加圧路
61 :加圧弁
70 :排気路
71 :排気弁
72 :逆止弁
80 :循環路
81 :循環ポンプ
82 :噴出ノズル
100 :給蒸路
101 :給蒸弁
110 :クーリングタワー
111 :送水ポンプ
112 :冷水送り路
113 :冷水戻し路
114 :冷水送り弁
115 :冷水戻し弁
130 :ドレン排出路
131 :ドレン排出弁
132 :スチームトラップ
133 :逆止弁
Reference Signs List 1: Sterilizer 2: Object to be treated 3: Treatment tank 4: Water supply means 5: Drainage means 6: Pressurization means 7: Exhaust means 8: Circulation means 9: Heat exchanger 10: Steam supply means 11: Main cooling means 13 : Drain discharge means 15 : Control means 16 : Abnormality detection means 16a : Differential pressure switch 16b : High pressure side connection port 16c : Low pressure side connection port 20 : Tray 40 : Water supply path 41 : Water supply pump 42 : Water supply valve 50 : Drainage path 51 : Drain valve 52 : Check valve 60 : Pressurization path 61 : Pressurization valve 70 : Exhaust path 71 : Exhaust valve 72 : Check valve 80 : Circulation path 81 : Circulation pump 82 : Ejection nozzle 100 : Steam supply path 101 : Supply Steam valve 110: Cooling tower 111: Water pump 112: Cold water feed path 113: Cold water return line 114: Cold water feed valve 115: Cold water return valve 130: Drain discharge line 131: Drain discharge valve 132: Steam trap 133: Check valve

Claims (6)

処理装置であって、
処理槽と、熱交換器と、異常検出手段と、補助冷却手段とを備え、
前記処理槽は、内部に収容された被処理物を、前記処理槽と前記熱交換器との間を循環する処理水により加熱又は冷却するよう構成され、
前記熱交換器は、前記処理水と流体との間の熱交換により前記処理水を冷却するよう構成され、
前記異常検出手段は、前記処理水又は前記流体の熱交換前後の状態量変化に基づき、又は前記流体の流量に基づき、前記熱交換器における冷却の異常を検出するよう構成され、
前記補助冷却手段は、前記異常が検出された場合に前記処理水を冷却するよう構成される、処理装置。
A processing device,
A treatment tank, a heat exchanger, an abnormality detection means, and an auxiliary cooling means,
The processing tank is configured to heat or cool the object to be processed contained therein with treated water circulating between the processing tank and the heat exchanger,
the heat exchanger is configured to cool the treated water by heat exchange between the treated water and a fluid;
The abnormality detection means is configured to detect a cooling abnormality in the heat exchanger based on a state quantity change before and after heat exchange of the treated water or the fluid, or based on the flow rate of the fluid,
The processing apparatus, wherein the auxiliary cooling means is configured to cool the treated water when the abnormality is detected.
請求項1に記載の処理装置であって、
前記異常検出手段は、前記流体の熱交換前後の圧力差に基づき前記異常を検出するよう構成される、処理装置。
The processing apparatus according to claim 1,
The processing device, wherein the abnormality detection means is configured to detect the abnormality based on a pressure difference before and after heat exchange of the fluid.
請求項1に記載の処理装置であって、
前記異常検出手段は、前記処理水の熱交換前後の温度差に基づき前記異常を検出するよう構成される、処理装置。
The processing apparatus according to claim 1,
The processing apparatus, wherein the abnormality detection means is configured to detect the abnormality based on a temperature difference between before and after heat exchange of the treated water.
請求項1に記載の処理装置であって、
前記異常検出手段は、前記流体の熱交換前後の温度差に基づき前記異常を検出するよう構成される、処理装置。
The processing apparatus according to claim 1,
The processing device, wherein the abnormality detection means is configured to detect the abnormality based on a temperature difference between before and after heat exchange of the fluid.
請求項1から請求項4のいずれか1つに記載の処理装置であって、
前記補助冷却手段は、前記処理槽、又は前記処理水の循環路に前記処理水を供給するよう構成された給水手段であり、
前記給水手段は、前記異常が検出された場合に前記処理水を追加で供給するよう構成される、処理装置。
The processing apparatus according to any one of claims 1 to 4,
The auxiliary cooling means is water supply means configured to supply the treated water to the treatment tank or the circulation path of the treated water,
The processing apparatus, wherein the water supply means is configured to additionally supply the treated water when the abnormality is detected.
請求項1から請求項4のいずれか1つに記載の処理装置であって、
主冷却手段を備え、
前記主冷却手段は、前記熱交換器に前記流体としての第1冷却水を供給するよう構成され、
前記補助冷却手段は、前記異常が検出された場合に前記熱交換器に第2冷却水を供給して前記処理水を冷却するよう構成される、処理装置。
The processing apparatus according to any one of claims 1 to 4,
comprising a main cooling means,
The main cooling means is configured to supply first cooling water as the fluid to the heat exchanger,
The processing apparatus, wherein the auxiliary cooling means is configured to supply second cooling water to the heat exchanger to cool the treated water when the abnormality is detected.
JP2022022027A 2022-02-16 2022-02-16 Processing device Pending JP2023119243A (en)

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Country Link
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