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JP6830237B2 - Vacuum cooling device - Google Patents
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JP6830237B2 - Vacuum cooling device - Google Patents

Vacuum cooling device Download PDF

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JP6830237B2
JP6830237B2 JP2016221130A JP2016221130A JP6830237B2 JP 6830237 B2 JP6830237 B2 JP 6830237B2 JP 2016221130 A JP2016221130 A JP 2016221130A JP 2016221130 A JP2016221130 A JP 2016221130A JP 6830237 B2 JP6830237 B2 JP 6830237B2
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heat exchanger
pipe
vacuum
upstream
wash water
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JP2018080846A (en
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伸基 明尾
伸基 明尾
西山 将人
将人 西山
森 寛
寛 森
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株式会社サムソン
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本発明は処理槽内を真空化し、処理槽内の被冷却物から水分を蒸発させた際に発生する気化熱を利用して被冷却物を冷却する真空冷却装置に関するものである。 The present invention relates to a vacuum cooling device that evacuates the inside of a treatment tank and cools the object to be cooled by utilizing the heat of vaporization generated when water is evaporated from the object to be cooled in the treatment tank.

処理槽内に加熱調理した食品などの被冷却物を収容しておき、処理槽内を真空化することで被冷却物を冷却する真空冷却装置がある。被冷却物を収容している処理槽内を減圧し、処理槽内での沸点を被冷却物の温度よりも低下させると、被冷却物中の水分が蒸発し、その際に被冷却物から気化熱を奪うため、被冷却物を短時間で冷却することができる。真空冷却装置に使用する真空発生装置としては、水又は蒸気によるエジェクタや水封式又はドライ式の真空ポンプによるものが知られている。真空発生装置にて処理槽内の気体を吸引する場合、吸引気体と同時に被冷却物から発生した蒸気も吸引することになる。しかし、水は液体から気体に変わると体積が大幅に増大するため、蒸気をそのまま真空発生装置に吸引させたのでは、真空発生装置で排出しなければならない気体量が多くなる。その場合、処理槽内の減圧に要する時間が長くなるため、冷却工程時間が長くなってしまう。 There is a vacuum cooling device that cools the object to be cooled by accommodating the object to be cooled such as cooked food in the processing tank and evacuating the inside of the processing tank. When the pressure inside the treatment tank containing the object to be cooled is reduced and the boiling point in the treatment tank is lowered below the temperature of the object to be cooled, the water content in the object to be cooled evaporates, and at that time, from the object to be cooled. Since the heat of vaporization is taken away, the object to be cooled can be cooled in a short time. As a vacuum generator used in the vacuum cooling device, an ejector using water or steam or a water-sealed or dry type vacuum pump is known. When the gas in the processing tank is sucked by the vacuum generator, the steam generated from the object to be cooled is also sucked at the same time as the sucked gas. However, since the volume of water increases significantly when it changes from a liquid to a gas, if the vapor is sucked into the vacuum generator as it is, the amount of gas that must be discharged by the vacuum generator increases. In that case, the time required for decompression in the treatment tank becomes long, so that the cooling process time becomes long.

そのため、特開2014−152982号公報に記載があるように、処理槽内の気体を真空発生装置へ送る真空配管の途中に、真空発生装置が吸引している気体を冷却する熱交換器を設け、真空配管の途中で気体を冷却することが行われている。熱交換器によって気体の冷却を行うと、気体の体積が縮小し、特に蒸気を冷却して液体に戻すと体積は大幅に小さくなるため、真空発生装置が吸引する気体の体積が小さくなり、真空冷却の効率を高めることができる。特開2014−152982号公報に記載の発明では、冷水ユニットによって製造した冷水をためる冷水タンク内に熱交換器の伝熱管を設置した構成であって、冷水タンクの上部から冷水部分を貫通させて冷水タンクの下部まで達するようにしている第一熱交換器と、冷水タンクの下部から冷水部分を貫通させて冷水タンクの上部まで達するようにしている第二熱交換器を設け、第一熱交換器と第二熱交換器は冷水タンクの下部で連結した構造としている。 Therefore, as described in Japanese Patent Application Laid-Open No. 2014-152982, a heat exchanger for cooling the gas sucked by the vacuum generator is provided in the middle of the vacuum pipe for sending the gas in the processing tank to the vacuum generator. , The gas is cooled in the middle of the vacuum pipe. When the gas is cooled by the heat exchanger, the volume of the gas is reduced, and especially when the steam is cooled and returned to the liquid, the volume is significantly reduced, so that the volume of the gas sucked by the vacuum generator becomes small, and the vacuum The efficiency of cooling can be increased. In the invention described in Japanese Patent Application Laid-Open No. 2014-152982, the heat transfer tube of the heat exchanger is installed in the cold water tank for storing the cold water produced by the cold water unit, and the cold water portion is penetrated from the upper part of the cold water tank. A first heat exchanger that reaches the bottom of the chilled water tank and a second heat exchanger that penetrates the chilled water part from the bottom of the chilled water tank to reach the top of the chilled water tank are provided for the first heat exchange. The vessel and the second heat exchanger are connected at the bottom of the cold water tank.

食品を冷却する真空冷却装置の場合、処理槽内だけでなく真空配管内や熱交換器内も清潔に保つことが必要であるが、熱交換器は内部の構造が複雑であるため洗浄し難い。そして、熱交換器内の殺菌を行う場合の殺菌方法としては、熱交換器内に蒸気や供給することができるようにしておき、熱によって殺菌することが行われていた。真空配管内を加熱することで殺菌を行うことができるが、熱交換器内の流路が長い、又は流路の構成部材の比熱が異なることによって温度ムラが発生するなどにより、殺菌が不十分になることがあるとの問題があった。また、真空冷却装置のドレン配管などの排水配管では、経済性によって塩ビ配管が用いられることが多いが、蒸気での加熱による殺菌を行う場合には、排水配管も耐熱性の配管施工が必要となるため、コストの上昇を招くことになることも問題であった。 In the case of a vacuum cooling device that cools food, it is necessary to keep not only the inside of the processing tank but also the inside of the vacuum piping and the heat exchanger clean, but the heat exchanger is difficult to clean due to the complicated internal structure. .. As a sterilization method for sterilizing the inside of the heat exchanger, steam or supply is provided in the heat exchanger and sterilization is performed by heat. Sterilization can be performed by heating the inside of the vacuum pipe, but sterilization is insufficient because the flow path in the heat exchanger is long or the specific heat of the components of the flow path is different, causing temperature unevenness. There was a problem that it could become. In addition, PVC pipes are often used for drainage pipes such as drain pipes of vacuum cooling devices due to economic efficiency, but when sterilizing by heating with steam, it is necessary to install heat-resistant pipes for the drainage pipes as well. Therefore, it was also a problem that the cost would increase.

特開2014−152982号公報Japanese Unexamined Patent Publication No. 2014-152982

本発明が解決しようとする課題は、真空冷却装置において、真空配管内の洗浄や殺菌をムラなく確実に行うことのできる真空冷却装置を提供することにある。 An object to be solved by the present invention is to provide a vacuum cooling device capable of reliably cleaning and sterilizing the inside of a vacuum pipe in a vacuum cooling device.

請求項1に記載の発明は、被冷却物を収容する処理槽、処理槽と真空配管によって接続しており処理槽内の気体を吸引する真空発生装置、真空発生装置が処理槽から吸引している気体を途中で冷却する熱交換器を持ち、処理槽内を真空化することで被冷却物の冷却を行う真空冷却装置であって、真空配管の熱交換器より上流側に洗浄水を供給する上流用洗浄水配管を接続し、上流用洗浄水配管の途中には上流用洗浄水配管から熱交換器へ洗浄用水を供給することができることを特徴とした真空冷却装置において、熱交換器へ共有した洗浄用水を排出する排水管には洗浄水の流出を止める排水遮断弁を設置しておき、熱交換器を洗浄する場合、排水遮断弁を開いて行う流水洗浄と排水遮断弁を閉じて行う漬け置き洗浄を行えるようにしていることを特徴としているThe invention according to claim 1 is a treatment tank for accommodating an object to be cooled, a vacuum generator which is connected to the treatment tank by a vacuum pipe and sucks gas in the treatment tank, and a vacuum generator sucks from the treatment tank. A vacuum cooling device that has a heat exchanger that cools the existing gas in the middle and cools the object to be cooled by vacuuming the inside of the processing tank, and supplies cleaning water to the upstream side of the heat exchanger of the vacuum piping. in the vacuum cooling device connected upstream cleaning water pipe, in the middle of the upstream cleaning water pipe which is characterized in that it is possible to supply the wash water from the upstream washing water pipe to the heat exchanger that, to the heat exchanger A drainage shutoff valve is installed in the drainage pipe that discharges the shared wash water to stop the outflow of washwater. When cleaning the heat exchanger, open the drainage shutoff valve and close the running water wash and drainage shutoff valve. It is characterized by being able to perform soaking and washing .

請求項2に記載の発明は、前記の真空冷却装置において、 熱交換器は、上流側の第一熱交換器と下流側の第二熱交換器の2段階としており、真空配管の第一熱交換器より上流側に接続する上流用洗浄水配管と、第二熱交換器より下流側に接続する下流用洗浄水配管を設置し、上流用洗浄水配管の途中には上流用洗浄水弁、下流用洗浄水配管の途中には下流用洗浄水弁を設置しておき、洗浄用水を、上流用洗浄水配管から第一熱交換器へと、下流用洗浄水配管から第二熱交換器へ供給することができるようにしたことを特徴とする。 According to the second aspect of the present invention, in the vacuum cooling device, the heat exchanger has two stages, the first heat exchanger on the upstream side and the second heat exchanger on the downstream side, and the first heat of the vacuum pipe. An upstream wash water pipe connected to the upstream side of the exchanger and a downstream wash water pipe connected to the downstream side of the second heat exchanger are installed, and an upstream wash water valve is installed in the middle of the upstream wash water pipe. A downstream wash water valve is installed in the middle of the downstream wash water pipe, and the wash water is transferred from the upstream wash water pipe to the first heat exchanger and from the downstream wash water pipe to the second heat exchanger. It is characterized by being able to supply.

請求項3に記載の発明は、前記の真空冷却装置において、上流用洗浄水配管及び下流用洗浄水配管の上流用洗浄水弁及び下流用洗浄水弁より上流側に、洗浄水に殺菌作用を持たせるための殺菌剤を添加する殺菌剤供給配管を接続していることを特徴とする。 The invention according to claim 3 exerts a bactericidal action on the washing water on the upstream side of the upstream washing water valve and the downstream washing water pipe and the downstream washing water valve in the vacuum cooling device. It is characterized by connecting a disinfectant supply pipe to which a disinfectant for holding is added.

請求項4に記載の発明は、前記の真空冷却装置において、熱交換器へ供給した洗浄用水を排出する排水管には洗浄水の流出を止める排水遮断弁を設置しておき、熱交換器を洗浄する場合、排水遮断弁を開いて行う流水洗浄と、排水遮断弁を閉じて行う浸け置き洗浄を行えるようにしていることを特徴とする。 According to the fourth aspect of the present invention, in the vacuum cooling device, a drainage shutoff valve for stopping the outflow of the washing water is installed in the drain pipe for discharging the washing water supplied to the heat exchanger, and the heat exchanger is installed. When cleaning, it is characterized in that it is possible to perform running water cleaning performed by opening the drainage shutoff valve and immersion cleaning performed by closing the drainage shutoff valve.

本発明を実施することで、真空配管の熱交換器内を洗浄殺菌することができ、被冷却物が汚染されることなく冷却することができる。 By carrying out the present invention, the inside of the heat exchanger of the vacuum pipe can be cleaned and sterilized, and the object to be cooled can be cooled without being contaminated.

本発明の一実施例における真空冷却装置のフロー図Flow chart of the vacuum cooling device in one embodiment of the present invention

本発明の一実施例を図面を用いて説明する。図1は本発明の実施例における真空冷却装置のフロー図である。真空冷却装置は、処理槽2、真空発生装置1、第一熱交換器4、第二熱交換器5、冷水ユニット3、冷水タンク10などからなっている。真空冷却装置は、処理槽2の内部を真空化することによって、処理槽2に収容した被冷却物(高温の食品)から水分を蒸発させ、その際に発生する気化熱の作用によって冷却を行う。 An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a flow chart of a vacuum cooling device according to an embodiment of the present invention. The vacuum cooling device includes a processing tank 2, a vacuum generator 1, a first heat exchanger 4, a second heat exchanger 5, a chilled water unit 3, a chilled water tank 10, and the like. The vacuum cooling device evacuates the inside of the treatment tank 2 to evaporate water from the object to be cooled (high temperature food) contained in the treatment tank 2, and cools the inside by the action of the heat of vaporization generated at that time. ..

処理槽2と真空発生装置1の間は、真空配管9によって接続しておき、真空発生装置1を作動することによって処理槽2内の気体を排出する。このとき、処理槽2内の気体とともに被冷却物から発生した蒸気も真空発生装置1で吸引するようにしていると、真空発生装置1が吸引しなければならない気体の容積が大きくなり、処理槽2内の減圧に時間が掛かることになるため、冷却時間が長くなる。そのため真空配管9の途中には熱交換器を設けておき、真空発生装置1が吸引している気体や気体中に含まれている蒸気を熱交換器で冷却することによって、吸引しなければならない気体の体積を縮小している。 The processing tank 2 and the vacuum generator 1 are connected by a vacuum pipe 9, and the gas in the processing tank 2 is discharged by operating the vacuum generator 1. At this time, if the vacuum generator 1 sucks the vapor generated from the object to be cooled together with the gas in the treatment tank 2, the volume of the gas that the vacuum generator 1 must suck becomes large, and the treatment tank Since it takes time to reduce the pressure in 2, the cooling time becomes long. Therefore, a heat exchanger must be provided in the middle of the vacuum pipe 9, and the gas sucked by the vacuum generator 1 and the vapor contained in the gas must be sucked by cooling with the heat exchanger. The volume of gas is reduced.

熱交換器は、上流側の第一熱交換器4と下流側の第二熱交換器5の2段階とし、冷水タンク10内に設けている。第一熱交換器4と下流側の第二熱交換器5の伝熱管は、冷水タンク10の水部を貫通させるようにして設置している。第一熱交換器4の上部には処理槽2から吸引してきた気体を第一熱交換器4の複数の伝熱管に分散させるための上部分散室、第二熱交換器5の上部には第二熱交換器5の複数の伝熱管を流れてきた気体を集合させる上部集合室を設ける。 The heat exchanger has two stages, a first heat exchanger 4 on the upstream side and a second heat exchanger 5 on the downstream side, and is provided in the cold water tank 10. The heat transfer tubes of the first heat exchanger 4 and the second heat exchanger 5 on the downstream side are installed so as to penetrate the water portion of the cold water tank 10. The upper part of the first heat exchanger 4 is an upper dispersion chamber for dispersing the gas sucked from the processing tank 2 in a plurality of heat transfer tubes of the first heat exchanger 4, and the upper part of the second heat exchanger 5 is the first. An upper assembly chamber for collecting the gas flowing through the plurality of heat transfer tubes of the two heat exchangers 5 is provided.

冷水タンク10は直方体形状であって、冷水ユニット3との間を冷却用水配管7によって接続しておき、冷水ユニット3で発生させた冷水をためておくものである。冷却用水配管7は、冷水ユニット3と冷水タンク10の間で冷水を循環させることができるようにしており、冷却用水配管7の途中には循環ポンプ8を設けている。冷水タンク10の下部には、第一熱交換器4の複数の伝熱管に分かれて流れてきた気体を集合させる下部集合室を設ける。下部集合室は、冷水タンク10の下部で気体流をターンさせて第二熱交換器5へ流すものであり、下部集合室の天井面は冷水タンクの底板としており、第一熱交換器4及び第二熱交換器5の伝熱管下端は下部集合室まで達する構成としている。下部集合室の底部にはドレン配管を接続しておき、熱交換器で発生した凝縮水(ドレン)はドレン配管を通して下方に設けているドレンタンク6へ送ることができるようにしておく。ドレン配管の途中には排水遮断弁19を設置しておき、排水遮断弁19の開閉で排水の操作を行う。 The chilled water tank 10 has a rectangular parallelepiped shape, and is connected to the chilled water unit 3 by a cooling water pipe 7 to store the chilled water generated by the chilled water unit 3. The cooling water pipe 7 is capable of circulating cold water between the cold water unit 3 and the cold water tank 10, and a circulation pump 8 is provided in the middle of the cooling water pipe 7. At the lower part of the chilled water tank 10, a lower collecting chamber for collecting the gas that has been divided into a plurality of heat transfer tubes of the first heat exchanger 4 and has flowed is provided. In the lower assembly chamber, a gas flow is turned at the lower part of the chilled water tank 10 and flows to the second heat exchanger 5. The ceiling surface of the lower assembly chamber is the bottom plate of the chilled water tank, and the first heat exchanger 4 and The lower end of the heat transfer tube of the second heat exchanger 5 is configured to reach the lower assembly chamber. A drain pipe is connected to the bottom of the lower assembly chamber so that the condensed water (drain) generated in the heat exchanger can be sent to the drain tank 6 provided below through the drain pipe. A drainage shutoff valve 19 is installed in the middle of the drain pipe, and the drainage is operated by opening and closing the drainage shutoff valve 19.

処理槽2からの真空配管9は第一熱交換器4の上部分散室に接続し、真空発生装置1へ接続している真空配管9は第二熱交換器5の上部集合室に接続しておき、処理槽2から吸引してきた気体は、第一熱交換器4と第二熱交換器5を通った後に真空発生装置1へ達するようにしておく。第一熱交換器4は上部分散室と下部集合室の間を多数の伝熱管でつなぎ、第二熱交換器5も上部集合室と下部集合室の間を多数の伝熱管でつないでいるものである。そのため、処理槽2から取り出された気体は、上部分散室から第一熱交換器4の伝熱管に分かれて進み、冷水タンク10の下方に設けている下部集合室に入ることで集合する。その後、下部集合室でターンした後に再び第二熱交換器5の伝熱管に分かれて進み、上部集合室13で集合した後に真空発生装置1に向かうことになる。第一熱交換器4及び第二熱交換器5の伝熱管は、冷水タンク10の水部を貫通させて設置しているため、伝熱管の外側は冷水タンク10の冷水に接している。 The vacuum pipe 9 from the processing tank 2 is connected to the upper dispersion chamber of the first heat exchanger 4, and the vacuum pipe 9 connected to the vacuum generator 1 is connected to the upper assembly chamber of the second heat exchanger 5. The gas sucked from the processing tank 2 is set to reach the vacuum generator 1 after passing through the first heat exchanger 4 and the second heat exchanger 5. The first heat exchanger 4 connects the upper dispersion chamber and the lower assembly chamber with a large number of heat transfer tubes, and the second heat exchanger 5 also connects the upper assembly chamber and the lower assembly chamber with a large number of heat transfer tubes. Is. Therefore, the gas taken out from the treatment tank 2 separates from the upper dispersion chamber into the heat transfer tube of the first heat exchanger 4 and collects by entering the lower gathering chamber provided below the chilled water tank 10. After that, after making a turn in the lower gathering chamber, the heat exchanger 5 is divided into heat transfer tubes again, and after gathering in the upper gathering chamber 13, it heads for the vacuum generator 1. Since the heat transfer tubes of the first heat exchanger 4 and the second heat exchanger 5 are installed so as to penetrate the water portion of the cold water tank 10, the outside of the heat transfer tubes is in contact with the cold water of the cold water tank 10.

真空配管9の処理槽2と第一熱交換器4の間に上流真空弁11、真空配管9の第二熱交換器5と真空発生装置1の間に下流真空弁12を設置しておき、真空配管9は上流真空弁11と下流真空弁12で閉鎖できるようにしている。また真空配管9には、第一熱交換器4および第二熱交換器5の洗浄と殺菌を行うための洗浄水配管を接続しておく。洗浄水配管は、真空配管9の上流真空弁11から第一熱交換器4までの間に接続する上流用洗浄水配管16と、第二熱交換器から下流真空弁12までの間に接続する下流用洗浄水配管17を設置している。上流用洗浄水配管16の接続部と、下流用洗浄水配管17の接続部は、第一熱交換器4及び第二熱交換器5よりも高い位置としておき、洗浄水は第一熱交換器4及び第二熱交換器5の上方から下方へ自然に流れるようにしておく。 An upstream vacuum valve 11 is installed between the processing tank 2 of the vacuum pipe 9 and the first heat exchanger 4, and a downstream vacuum valve 12 is installed between the second heat exchanger 5 of the vacuum pipe 9 and the vacuum generator 1. The vacuum pipe 9 can be closed by the upstream vacuum valve 11 and the downstream vacuum valve 12. Further, a cleaning water pipe for cleaning and sterilizing the first heat exchanger 4 and the second heat exchanger 5 is connected to the vacuum pipe 9. The wash water pipe is connected between the upstream wash water pipe 16 connected between the upstream vacuum valve 11 of the vacuum pipe 9 and the first heat exchanger 4 and between the second heat exchanger and the downstream vacuum valve 12. A downstream wash water pipe 17 is installed. The connection part of the upstream wash water pipe 16 and the connection part of the downstream wash water pipe 17 are set at higher positions than the first heat exchanger 4 and the second heat exchanger 5, and the wash water is the first heat exchanger. Allow the water to flow naturally from above to below the 4 and the second heat exchanger 5.

そして上流用洗浄水配管16の途中には上流用洗浄水弁13、下流用洗浄水配管17の途中には下流用洗浄水弁14を設置しておき、洗浄水を流す時のみ上流用洗浄水弁13と下流用洗浄水弁14を開くようにしておく。上流用洗浄水配管16及び下流用洗浄水配管17の上流用洗浄水弁13及び下流用洗浄水弁14より上流側部分には、洗浄水に殺菌作用を持たせるための殺菌剤を添加する殺菌剤供給配管18を設置している。洗浄水に殺菌作用をもたせるために添加するものとしては、次亜塩素酸ナトリウムが広く用いられている。もちろん殺菌作用のあるものであればよいため、この殺菌剤は次亜塩素酸ナトリウムに限られるものではない。また、殺菌剤供給配管18を通して中性洗剤等の洗浄成分も添加できるようにしておいてもよい。殺菌剤供給配管18には殺菌剤供給弁15を設置しており、殺菌剤供給弁15によって殺菌剤の供給を調節する。 An upstream wash water valve 13 is installed in the middle of the upstream wash water pipe 16, and a downstream wash water valve 14 is installed in the middle of the downstream wash water pipe 17, and the upstream wash water is only flowed. The valve 13 and the downstream wash water valve 14 are opened. Sterilization by adding a sterilizing agent to give the washing water a bactericidal action to the upstream washing water valve 13 and the downstream washing water valve 14 of the upstream washing water pipe 16 and the downstream washing water pipe 17. The agent supply pipe 18 is installed. Sodium hypochlorite is widely used as an addition to wash water to have a bactericidal action. Of course, this bactericidal agent is not limited to sodium hypochlorite as long as it has a bactericidal action. Further, a cleaning component such as a neutral detergent may be added through the disinfectant supply pipe 18. A disinfectant supply valve 15 is installed in the disinfectant supply pipe 18, and the disinfectant supply valve 15 regulates the supply of the disinfectant.

実施例での運転動作を説明する。真空冷却をする場合は、処理槽2内に被冷却物を収容し、処理槽2を密閉しておく。上流用洗浄水弁13、下流用洗浄水弁14、殺菌剤供給弁15は、洗浄時に開くものであり、冷却時には閉じておく。真空発生装置1、冷水ユニット3、循環ポンプ8の各機器類を作動することで真空冷却運転を行うと、処理槽2内の気体が真空配管9を通して真空発生装置1から取り出され、処理槽2内の圧力が低下していく。処理槽内の圧力が低下すると、処理槽2内に収容している被冷却物から水分が蒸発し、水分が蒸発する際には周囲から気化熱を奪うため、被冷却物の温度は急激に低下していく。 The driving operation in the embodiment will be described. When vacuum cooling is performed, the object to be cooled is housed in the processing tank 2 and the processing tank 2 is sealed. The upstream wash water valve 13, the downstream wash water valve 14, and the disinfectant supply valve 15 are opened at the time of cleaning and are closed at the time of cooling. When the vacuum cooling operation is performed by operating the vacuum generator 1, the chilled water unit 3, and the circulation pump 8, the gas in the processing tank 2 is taken out from the vacuum generator 1 through the vacuum pipe 9, and the processing tank 2 is used. The pressure inside decreases. When the pressure in the treatment tank drops, the moisture evaporates from the object to be cooled contained in the treatment tank 2, and when the moisture evaporates, the heat of vaporization is taken from the surroundings, so that the temperature of the object to be cooled suddenly rises. It will decrease.

真空配管9を通して送られてきた気体は、第一熱交換器4の上部分散室から複数の伝熱管に分岐して下向きに流れ、下部集合室へ向かう。伝熱管は低温の冷水をためた冷水タンク10に設置しているものであり、伝熱管の外側表面は冷水に接しているために伝熱管では周囲から冷却されている。そのため伝熱管内を流れる気体は、伝熱管の周囲から冷却されながら進むことになる。第一熱交換器4内を下向きに流れた気体は、下部集合室でターンして第二熱交換器5内を上向きに流れる。第二熱交換器5の伝熱管も周囲で冷水と接しているために第二熱交換器5内を流れる気体は更に冷却される。 The gas sent through the vacuum pipe 9 branches from the upper dispersion chamber of the first heat exchanger 4 to a plurality of heat transfer tubes, flows downward, and heads for the lower assembly chamber. The heat transfer tube is installed in a cold water tank 10 that stores low-temperature cold water, and since the outer surface of the heat transfer tube is in contact with the cold water, the heat transfer tube is cooled from the surroundings. Therefore, the gas flowing in the heat transfer tube travels while being cooled from the periphery of the heat transfer tube. The gas that has flowed downward in the first heat exchanger 4 turns in the lower assembly chamber and flows upward in the second heat exchanger 5. Since the heat transfer tube of the second heat exchanger 5 is also in contact with cold water in the surroundings, the gas flowing in the second heat exchanger 5 is further cooled.

第一熱交換器4及び第二熱交換器5で気体の冷却を行うと、気体中に含まれていた蒸気が凝縮し、凝縮水は伝熱管内側表面を伝わり落ちて伝熱管の下方にある下部集合室へ流れ落ちる。下部集合室の底部に流れ落ちた凝縮水は、下部集合室の底部に接続しているドレン配管を通して下方に設置しているドレンタンク6へ流れ落ちていく。蒸気が凝縮水になると体積は大幅に小さくなるため、処理槽2から吸引してきた気体は第一熱交換器4で体積を縮小させ、第二熱交換器5でさらに体積を縮小させる。そのため、第二熱交換器5で必要な気体流路の断面積は、第一熱交換器4に比べると小さくなっており、第二熱交換器の伝熱管設置数は第一熱交換器4よりも少なくすることができる。気体の体積が小さくなると、真空発生装置1で排出しなければならない気体量が少なくなるため、より早く処理槽2内の圧力を低下することができ、冷却に要する時間を短縮させることができる。冷却が終了すると、真空発生装置1などを停止し、処理槽2内に大気を導入することで処理槽内を大気圧に戻す。処理槽内が大気圧に戻ると、処理槽の扉を開くことができるようになり、処理槽2内から被冷却物を取り出すことができる。 When the gas is cooled by the first heat exchanger 4 and the second heat exchanger 5, the steam contained in the gas is condensed, and the condensed water is transmitted down the inner surface of the heat transfer tube and is below the heat transfer tube. It flows down to the lower meeting room. The condensed water that has flowed down to the bottom of the lower assembly chamber flows down to the drain tank 6 installed below through the drain pipe connected to the bottom of the lower assembly chamber. When the steam becomes condensed water, the volume becomes significantly smaller. Therefore, the volume of the gas sucked from the treatment tank 2 is reduced by the first heat exchanger 4 and further reduced by the second heat exchanger 5. Therefore, the cross-sectional area of the gas flow path required for the second heat exchanger 5 is smaller than that of the first heat exchanger 4, and the number of heat transfer tubes installed in the second heat exchanger is smaller than that of the first heat exchanger 4. Can be less than. When the volume of the gas becomes small, the amount of gas that must be discharged by the vacuum generator 1 decreases, so that the pressure in the processing tank 2 can be reduced more quickly, and the time required for cooling can be shortened. When the cooling is completed, the vacuum generator 1 and the like are stopped, and the inside of the treatment tank is returned to the atmospheric pressure by introducing the atmosphere into the treatment tank 2. When the inside of the treatment tank returns to the atmospheric pressure, the door of the treatment tank can be opened, and the object to be cooled can be taken out from the inside of the treatment tank 2.

1日の冷却工程が終了した後のタイミングで真空冷却装置の洗浄を行う。第一熱交換器4及び第二熱交換器5で洗浄や殺菌を行う場合、上流真空弁11と下流真空弁12は閉じておき、上流用洗浄水弁13と下流用洗浄水配管17を開くことで洗浄水の供給を行う。洗浄の場合は水に洗剤を添加した洗浄水を供給し、殺菌の場合は水に殺菌剤を添加した殺菌用水を供給する。殺菌する場合は殺菌剤供給弁15を開くことで洗浄水に次亜塩素酸ナトリウム等の殺菌剤を添加して洗浄水に殺菌作用を持たせる。洗浄水(殺菌水)は、上流用洗浄水配管16を通して上流真空弁11と第一熱交換器4の間に送るものと、下流用洗浄水配管17を通して第二熱交換器5と下流真空弁12の間に送るものの2系統で供給する。図中では洗浄水の流れは黒塗りの矢印で示している。 The vacuum cooling device is cleaned at the timing after the cooling process of one day is completed. When cleaning or sterilizing with the first heat exchanger 4 and the second heat exchanger 5, the upstream vacuum valve 11 and the downstream vacuum valve 12 are closed, and the upstream cleaning water valve 13 and the downstream cleaning water pipe 17 are opened. By doing so, the washing water is supplied. In the case of washing, washing water in which a detergent is added to water is supplied, and in the case of sterilization, sterilizing water in which a sterilizing agent is added to water is supplied. When sterilizing, the disinfectant supply valve 15 is opened to add a disinfectant such as sodium hypochlorite to the cleaning water to give the cleaning water a bactericidal action. The wash water (sterilized water) is sent between the upstream vacuum valve 11 and the first heat exchanger 4 through the upstream wash water pipe 16, and the second heat exchanger 5 and the downstream vacuum valve through the downstream wash water pipe 17. It is supplied in two systems, although it is sent between twelve. In the figure, the flow of wash water is indicated by black arrows.

上流用洗浄水配管16を通して送った洗浄水は、第一熱交換器4の上部に設けている上部分散室に入って、上部分散室と接続している複数の伝熱管に分散し、伝熱管内を下向きに流れて伝熱管の下方にある下部集合室へ流れ落ちる。下流用洗浄水配管17を通して送った洗浄水は、第二熱交換器5の上部に設けている上部集合室に入って、上部集合室と接続している複数の伝熱管に分散し、伝熱管内を下向きに流れて伝熱管の下方にある下部集合室へ流れ落ちる。洗浄水はその後、下部集合室からドレンタンク6へ流れ落ち、ドレンの排出と同様のルートで排水される。下部集合室とドレンタンク6の間で配管に設置している排水遮断弁19を開いていると、洗浄は流水洗浄となり、排水遮断弁19を閉鎖しておけば、第一熱交換器4と第二熱交換器5を浸け置き洗浄(殺菌)することができる。またドレンタンク6の下流側で配管を閉鎖すればドレンタンク6も含めて浸け置き洗浄(殺菌)することができる。 The wash water sent through the upstream wash water pipe 16 enters the upper dispersion chamber provided in the upper part of the first heat exchanger 4, is dispersed in a plurality of heat transfer tubes connected to the upper dispersion chamber, and transfers heat. It flows downward in the pipe and flows down to the lower assembly chamber below the heat transfer pipe. The wash water sent through the downstream wash water pipe 17 enters the upper assembly chamber provided in the upper part of the second heat exchanger 5, is dispersed in a plurality of heat transfer tubes connected to the upper assembly chamber, and transfers heat. It flows downward in the pipe and flows down to the lower assembly chamber below the heat transfer pipe. The wash water then flows down from the lower assembly chamber to the drain tank 6 and is drained by the same route as the drain discharge. If the drainage shutoff valve 19 installed in the pipe between the lower assembly room and the drain tank 6 is opened, the cleaning will be running water cleaning, and if the drainage shutoff valve 19 is closed, the first heat exchanger 4 and The second heat exchanger 5 can be immersed and washed (sterilized). Further, if the pipe is closed on the downstream side of the drain tank 6, the drain tank 6 can be immersed and washed (sterilized).

殺菌剤を含んだ洗浄水を上流用洗浄水配管16と下流用洗浄水配管17の2系統から供給することで、殺菌ムラを発生することなく、第一熱交換器4と第二熱交換器5の全体を殺菌することができる。また、洗浄水配管は上流用洗浄水配管16と下流用洗浄水配管17に分岐しているが、洗浄水の供給を制御する洗浄水弁は、上流用洗浄水配管16と下流用洗浄水配管17に分岐した以降の部分に設置する。そして殺菌剤供給配管18は、上流用洗浄水弁13および下流用洗浄水弁14より上流側の洗浄水配管に接続する。 By supplying the washing water containing the sterilizing agent from the upstream washing water pipe 16 and the downstream washing water pipe 17, the first heat exchanger 4 and the second heat exchanger 4 and the second heat exchanger do not cause uneven sterilization. The whole of 5 can be sterilized. The wash water pipe is branched into an upstream wash water pipe 16 and a downstream wash water pipe 17, but the wash water valve for controlling the supply of wash water is an upstream wash water pipe 16 and a downstream wash water pipe. It is installed in the part after branching to 17. The disinfectant supply pipe 18 is connected to the washing water pipe on the upstream side of the upstream washing water valve 13 and the downstream washing water valve 14.

洗浄水の供給を制御するだけであれば、洗浄水弁は分岐前の洗浄水配管に設置してもよいが、分岐前の洗浄水配管に洗浄水弁を設置した場合、真空配管9の第一熱交換器4よりも上流側と第二熱交換器5よりも下流側が、上流用洗浄水配管16と下流用洗浄水配管17によって繋がることになる。その場合、真空冷却工程時には、処理槽2から吸引してきた空気が洗浄水配管内を流れ、第一熱交換器4及び第二熱交換器5を通らずに真空発生装置1へ送られることになり、空気流量を冷却することによる体積の縮小が行えないため、減圧の効率が低下することになる。 If only controlling the supply of wash water, the wash water valve may be installed in the wash water pipe before branching, but if the wash water valve is installed in the wash water pipe before branching, the first of the vacuum pipe 9. The upstream side of the one heat exchanger 4 and the downstream side of the second heat exchanger 5 are connected by the upstream wash water pipe 16 and the downstream wash water pipe 17. In that case, during the vacuum cooling step, the air sucked from the processing tank 2 flows in the cleaning water pipe and is sent to the vacuum generator 1 without passing through the first heat exchanger 4 and the second heat exchanger 5. Therefore, the volume cannot be reduced by cooling the air flow rate, so that the efficiency of decompression is reduced.

分岐後の上流用洗浄水配管16と下流用洗浄水配管17にそれぞれ上流用洗浄水弁13と下流用洗浄水弁14を設置し、殺菌剤供給配管18も上流用洗浄水弁13及び下流用洗浄水弁14より上流側に設置したものであると、真空冷却工程時に処理槽2から吸引してきた空気は、上流用洗浄水弁13及び下流用洗浄水弁14によって閉鎖されているために洗浄水配管の上流側を回ることはなくなる。そのため、処理槽2から吸引してきた空気は、第一熱交換器4と第二熱交換器5を通って冷却されることになり、空気の体積を縮小することができるため、効率よく減圧を行うことができ、冷却に要する時間を短縮することができる。 An upstream wash water valve 13 and a downstream wash water valve 14 are installed in the upstream wash water pipe 16 and the downstream wash water pipe 17 after branching, respectively, and the disinfectant supply pipe 18 is also used for the upstream wash water valve 13 and the downstream. If it is installed on the upstream side of the wash water valve 14, the air sucked from the treatment tank 2 during the vacuum cooling step is washed because it is closed by the upstream wash water valve 13 and the downstream wash water valve 14. It will not go around the upstream side of the water pipe. Therefore, the air sucked from the processing tank 2 is cooled through the first heat exchanger 4 and the second heat exchanger 5, and the volume of air can be reduced, so that the pressure can be reduced efficiently. This can be done and the time required for cooling can be shortened.

なお、本発明は以上説明した実施例に限定されるものではなく、多くの変形が本発明の技術的思想内で当分野において通常の知識を有する者により可能である。 The present invention is not limited to the examples described above, and many modifications can be made by a person having ordinary knowledge in the art within the technical idea of the present invention.

1 真空発生装置
2 処理槽
3 冷水ユニット
4 第一熱交換器
5 第二熱交換器
6 ドレンタンク
7 冷却用水配管
8 循環ポンプ
9 真空配管
10 冷水タンク
11 上流真空弁
12 下流真空弁
13 上流用洗浄水弁
14 下流用洗浄水弁
15 殺菌剤供給弁
16 上流用洗浄水配管
17 下流用洗浄水配管
18 殺菌剤供給配管
19 排水遮断弁
1 Vacuum generator
2 Treatment tank
3 Cold water unit
4 First heat exchanger
5 Second heat exchanger
6 Drain tank
7 Cooling water piping
8 Circulation pump
9 Vacuum piping
10 Cold water tank
11 Upstream vacuum valve
12 Downstream vacuum valve
13 Upstream wash water valve
14 Downstream wash water valve 15 Disinfectant supply valve 16 Upstream wash water pipe 17 Downstream wash water pipe 18 Disinfectant supply pipe 19 Drainage shutoff valve

Claims (4)

被冷却物を収容する処理槽、処理槽と真空配管によって接続しており処理槽内の気体を吸引する真空発生装置、真空発生装置が処理槽から吸引している気体を途中で冷却する熱交換器を持ち、処理槽内を真空化することで被冷却物の冷却を行う真空冷却装置であって、真空配管の熱交換器より上流側に洗浄水を供給する上流用洗浄水配管を接続し、上流用洗浄水配管の途中には上流用洗浄水配管から熱交換器へ洗浄用水を供給することができることを特徴とした真空冷却装置において、熱交換器へ共有した洗浄用水を排出する排水管には洗浄水の流出を止める排水遮断弁を設置しておき、熱交換器を洗浄する場合、排水遮断弁を開いて行う流水洗浄と排水遮断弁を閉じて行う漬け置き洗浄を行えるようにしていることを特徴としている真空冷却装置A treatment tank that houses the object to be cooled, a vacuum generator that is connected to the treatment tank by a vacuum pipe and sucks the gas in the treatment tank, and a heat exchange that cools the gas sucked from the treatment tank on the way. It is a vacuum cooling device that cools the object to be cooled by holding a container and vacuuming the inside of the processing tank, and connects the upstream cleaning water pipe that supplies cleaning water to the upstream side from the heat exchanger of the vacuum pipe. In the vacuum cooling system , which is characterized by being able to supply cleaning water from the upstream cleaning water pipe to the heat exchanger in the middle of the upstream cleaning water pipe, a drain pipe that discharges the shared cleaning water to the heat exchanger. A drainage shutoff valve is installed in the pipe to stop the outflow of wash water, and when cleaning the heat exchanger, the drainage shutoff valve can be opened for running water cleaning and the drainage shutoff valve can be closed for soaking cleaning. A vacuum cooling device that is characterized by its presence . 請求項1に記載の真空冷却装置において、熱交換器は、上流側の第一熱交換器と下流側の第二熱交換器の2段階としており、真空配管の第一熱交換器より上流側に接続する上流用洗浄水配管と、第二熱交換器より下流側に接続する下流用洗浄水配管を設置し、上流用洗浄水配管の途中には上流用洗浄水弁、下流用洗浄水配管の途中には下流用洗浄水弁を設置しておき、洗浄用水を、上流用洗浄水配管から第一熱交換器へと、下流用洗浄水配管から第二熱交換器へ供給することができるようにしたことを特徴とする真空冷却装置。 In the vacuum cooling device according to claim 1, the heat exchanger has two stages, the first heat exchanger on the upstream side and the second heat exchanger on the downstream side, and is on the upstream side of the first heat exchanger of the vacuum pipe. An upstream wash water pipe connected to and a downstream wash water pipe connected to the downstream side of the second heat exchanger are installed, and an upstream wash water valve and a downstream wash water pipe are installed in the middle of the upstream wash water pipe. A downstream wash water valve can be installed in the middle of the process to supply wash water from the upstream wash water pipe to the first heat exchanger and from the downstream wash water pipe to the second heat exchanger. A vacuum cooling device characterized by the above. 請求項2に記載の真空冷却装置において、上流用洗浄水配管及び下流用洗浄水配管の上流用洗浄水弁及び下流用洗浄水弁より上流側に、洗浄水に殺菌作用を持たせるための殺菌剤を添加する殺菌剤供給配管を接続していることを特徴とする真空冷却装置。 In the vacuum cooling device according to claim 2, sterilization for giving the washing water a bactericidal action on the upstream side of the upstream washing water valve and the downstream washing water pipe and the downstream washing water valve. A vacuum cooling device characterized in that a disinfectant supply pipe to which an agent is added is connected. 請求項1から3のいずれかに記載の真空冷却装置において、熱交換器へ供給した洗浄用水を排出する排水管には洗浄水の流出を止める排水遮断弁を設置しておき、熱交換器を洗浄する場合、排水遮断弁を開いて行う流水洗浄と、排水遮断弁を閉じて行う浸け置き洗浄を行えるようにしていることを特徴とする真空冷却装置。

In the vacuum cooling device according to any one of claims 1 to 3, a drain shutoff valve for stopping the outflow of the washing water is installed in the drain pipe for discharging the washing water supplied to the heat exchanger, and the heat exchanger is installed. When cleaning, a vacuum cooling device characterized in that it is possible to perform running water cleaning performed by opening the drain shutoff valve and immersion cleaning performed by closing the drain shutoff valve.

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JPS5919918Y2 (en) * 1981-10-05 1984-06-08 株式会社トキメック Cleaning equipment for waste heat recovery equipment
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