JP7035541B2 - Vacuum defroster - Google Patents

Vacuum defroster Download PDF

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JP7035541B2
JP7035541B2 JP2018003899A JP2018003899A JP7035541B2 JP 7035541 B2 JP7035541 B2 JP 7035541B2 JP 2018003899 A JP2018003899 A JP 2018003899A JP 2018003899 A JP2018003899 A JP 2018003899A JP 7035541 B2 JP7035541 B2 JP 7035541B2
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JP2019122275A (en
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修士 加藤
泰範 狩野
久美 松矢
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Miura Co Ltd
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Description

本発明は、低圧蒸気により被解凍物の解凍を図る真空解凍装置に関するものである。 The present invention relates to a vacuum defrosting device for thawing an object to be thawed with low pressure steam.

従来、下記特許文献1に開示されるように、低圧蒸気により被解凍物の解凍を図る真空解凍装置が知られている。当該文献の図面に基づき説明すると、真空解凍装置は、被解凍物が収容される処理槽(解凍室2)と、処理槽内を吸引排気して減圧する減圧手段(4)と、ボイラ(リボイラ11)からの蒸気を処理槽内へ供給する給蒸手段(3)と、減圧下の処理槽内に外気を導入して復圧する復圧手段(5)とを備える。そして、真空解凍装置は、処理槽内から空気を排除する空気排除工程の後、減圧下の処理槽内へ蒸気を供給して被解凍物を解凍する解凍処理工程を実行する。 Conventionally, as disclosed in Patent Document 1 below, a vacuum thawing device for thawing an object to be thawed with low-pressure steam is known. Explaining based on the drawings of the document, the vacuum thawing device includes a processing tank (thawing chamber 2) in which an object to be defrosted is housed, a depressurizing means (4) for sucking and exhausting the inside of the processing tank to reduce the pressure, and a boiler (riboira). It is provided with a steaming means (3) for supplying the steam from 11) into the processing tank and a depressurizing means (5) for introducing outside air into the processing tank under reduced pressure to repressurize. Then, the vacuum defrosting device executes a defrosting process of supplying steam to the decompressed processing tank to thaw the object to be thawed after the air removing step of removing air from the processing tank.

特開2005-237633号公報Japanese Unexamined Patent Publication No. 2005-237633

従来技術では、給蒸手段は、ボイラから処理槽内への給蒸路に給蒸弁を備え、給蒸弁を開けることで、ボイラからの蒸気を処理槽内へ供給する。この場合、給蒸弁の前後(言い換えればボイラと処理槽)で圧力が異なることになる。そのため、次のような問題点があった。 In the prior art, the steaming means is provided with a steaming valve in the steaming path from the boiler to the inside of the processing tank, and the steam from the boiler is supplied into the processing tank by opening the steaming valve. In this case, the pressure will be different before and after the steam supply valve (in other words, the boiler and the processing tank). Therefore, there are the following problems.

すなわち、処理槽内を減圧後、給蒸弁を開けて処理槽内へ蒸気を吹き込む際、圧力配管としての給蒸路から減圧下の処理槽内に蒸気が放出される。そのため、吹き込み口付近では、吹き込まれた蒸気が過熱蒸気(過加熱蒸気)となり、解凍温度を大きく上回る温度領域が発生するおそれがある。このような事態は、一時的であるにしても、槽内温度の上昇や温度ムラ発生の要因となるおそれがあり、その解消が望まれる。 That is, after depressurizing the inside of the treatment tank, when the steam supply valve is opened and steam is blown into the treatment tank, the steam is discharged from the steam supply passage as a pressure pipe into the treatment tank under reduced pressure. Therefore, in the vicinity of the blow port, the blown steam becomes superheated steam (superheated steam), and there is a possibility that a temperature region far exceeding the thawing temperature may be generated. Even if it is temporary, such a situation may cause an increase in the temperature inside the tank and the occurrence of temperature unevenness, and it is desired to eliminate it.

そこで、本発明が解決しようとする課題は、処理槽内で蒸気が過熱されるのを防止して、所望温度でムラなく被解凍物を加熱できる真空解凍装置を提供することにある。 Therefore, an object to be solved by the present invention is to provide a vacuum defrosting device capable of preventing the steam from being overheated in the treatment tank and heating the object to be thawed evenly at a desired temperature.

本発明は、前記課題を解決するためになされたもので、請求項1に記載の発明は、被解凍物が収容される処理槽と、前記処理槽内の気体を外部へ吸引排出して前記処理槽内を減圧する減圧手段と、前記処理槽内と連通して設けられ、前記処理槽を介して前記減圧手段に接続され、貯留水が加熱されることで前記処理槽内へ蒸気を供給可能な蒸気発生タンクとを備え、前記蒸気発生タンク内の圧力に基づき、前記減圧手段による減圧と、前記蒸気発生タンクでの蒸気発生とを制御することを特徴とする真空解凍装置である。 The present invention has been made to solve the above problems, and the invention according to claim 1 is the treatment tank in which the object to be thawed is housed and the gas in the treatment tank is sucked and discharged to the outside. A depressurizing means for depressurizing the inside of the treatment tank and a depressurizing means provided in communication with the inside of the treatment tank, connected to the decompression means via the treatment tank, and heating the stored water to supply steam into the treatment tank. It is a vacuum defrosting apparatus including a possible steam generating tank, and controlling depressurization by the depressurizing means and steam generation in the steam generating tank based on the pressure in the steam generating tank .

請求項1に記載の発明によれば、蒸気発生タンク内が処理槽内と連通して設けられる。この場合、減圧手段により処理槽内を減圧すると、蒸気発生タンク内も同等圧力に減圧される。蒸気発生タンクでは処理槽内の圧力に応じた飽和蒸気が発生するため、その蒸気を処理槽内へ供給しても、処理槽内で過熱が生じるおそれがなく、所望温度でムラなく被解凍物を加熱することができる。
請求項1に記載の発明によれば、処理槽および蒸気発生タンク内の圧力ひいては温度を所望に調整して、所望温度でムラなく被解凍物を加熱することができる。
According to the first aspect of the present invention, the inside of the steam generation tank is provided so as to communicate with the inside of the treatment tank. In this case, when the inside of the treatment tank is depressurized by the depressurizing means, the inside of the steam generation tank is also depressurized to the same pressure. In the steam generation tank, saturated steam is generated according to the pressure in the treatment tank, so even if the steam is supplied into the treatment tank, there is no risk of overheating in the treatment tank, and the product to be thawed evenly at the desired temperature. Can be heated.
According to the first aspect of the present invention, the pressure in the treatment tank and the steam generation tank, and thus the temperature, can be adjusted as desired to heat the thawed material evenly at the desired temperature.

請求項2に記載の発明は、前記蒸気発生タンクは、貯留水中に蒸気が吹き込まれることで蒸気を発生させることを特徴とする請求項1に記載の真空解凍装置である。 The invention according to claim 2 is the vacuum defrosting apparatus according to claim 1, wherein the steam generating tank is characterized in that steam is generated by blowing steam into the stored water.

請求項2に記載の発明によれば、蒸気発生タンクの貯留水中に蒸気を吹き込んで加熱することができる。処理槽内の減圧に伴い蒸気発生タンク内も所定に減圧された状態で、蒸気発生タンク内の貯留水に蒸気を吹き込むと、吹き込まれた蒸気は貯留水に熱を伝えて飽和蒸気になると共に、貯留水は蒸気発生タンクの圧力(処理槽内の減圧)に応じた温度で減圧沸騰し飽和蒸気を発生する。これにより、蒸気の過熱を防止して、所望温度でムラなく被解凍物を加熱することができる。 According to the second aspect of the present invention, steam can be blown into the stored water of the steam generation tank to heat it. When steam is blown into the stored water in the steam generation tank while the steam generation tank is also depressurized as the pressure in the treatment tank is reduced, the blown steam transfers heat to the stored water and becomes saturated steam. , The stored water boils under reduced pressure at a temperature corresponding to the pressure of the steam generation tank (decompression in the treatment tank) to generate saturated steam. This makes it possible to prevent the steam from overheating and evenly heat the object to be thawed at a desired temperature.

請求項3に記載の発明は、前記蒸気発生タンクは、貯留水がヒータで加熱されることで蒸気を発生させることを特徴とする請求項1に記載の真空解凍装置である。 The invention according to claim 3 is the vacuum defrosting apparatus according to claim 1, wherein the steam generating tank is characterized in that steam is generated by heating stored water with a heater.

請求項3に記載の発明によれば、蒸気発生タンク内の貯留水をヒータで加熱することができる。処理槽内の減圧に伴い蒸気発生タンク内も所定に減圧された状態で、蒸気発生タンク内の貯留水を加熱すると、圧力に応じた目標温度で減圧沸騰した飽和蒸気を処理槽内へ供給することができる。これにより、蒸気の過熱を防止して、所望温度でムラなく被解凍物を加熱することができる。 According to the third aspect of the present invention, the stored water in the steam generation tank can be heated by a heater. When the stored water in the steam generation tank is heated while the steam generation tank is also depressurized as the pressure in the treatment tank is reduced, saturated steam boiled under reduced pressure at the target temperature according to the pressure is supplied to the treatment tank. be able to. This makes it possible to prevent the steam from overheating and evenly heat the object to be thawed at a desired temperature.

本発明の真空解凍装置によれば、処理槽内で蒸気が過熱されるのを防止して、所望温度でムラなく被解凍物を加熱することができる。 According to the vacuum thawing apparatus of the present invention, it is possible to prevent the steam from being overheated in the treatment tank and to heat the object to be thawed evenly at a desired temperature.

本発明の一実施例の真空解凍装置の概略図である。It is a schematic diagram of the vacuum defrosting apparatus of one Example of this invention.

以下、本発明の具体的実施例を図面に基づいて詳細に説明する。
図1は、本発明の一実施例の真空解凍装置1を示す概略図である。
Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic view showing a vacuum defrosting device 1 according to an embodiment of the present invention.

本実施例の真空解凍装置1は、被解凍物が収容される処理槽2と、この処理槽2内の気体を外部へ吸引排出して処理槽2内を減圧する減圧手段3と、処理槽2内と連通して設けられる蒸気発生タンク4と、減圧された処理槽2内へ外気を導入して処理槽2内を復圧する復圧手段5と、制御手段(図示省略)とを備える。 The vacuum defrosting device 1 of the present embodiment includes a processing tank 2 in which an object to be thawed is housed, a decompression means 3 for sucking and discharging the gas in the processing tank 2 to the outside to reduce the pressure in the processing tank 2, and a processing tank. It is provided with a steam generating tank 4 provided in communication with the inside of 2, a decompression means 5 for introducing outside air into the depressurized treatment tank 2 to repressurize the inside of the treatment tank 2, and a control means (not shown).

処理槽2は、被解凍物が収容される中空容器であり、扉で開閉可能とされる。たとえば、処理槽2は、略矩形の中空ボックス状に形成され、正面が扉で開閉可能とされる。処理槽2には、逆止弁からなる加圧解除弁6が設けられており、万一、処理槽2内が加圧される場合には、加圧解除弁6が自力で開いて、処理槽2内の圧力が大気圧に開放される。なお、処理槽2の底部には、所望により蒸気トラップなどを設けてもよい。 The processing tank 2 is a hollow container in which an object to be thawed is stored, and can be opened and closed by a door. For example, the processing tank 2 is formed in a substantially rectangular hollow box shape, and the front surface can be opened and closed by a door. The processing tank 2 is provided with a pressure release valve 6 composed of a check valve. In the unlikely event that the inside of the processing tank 2 is pressurized, the pressure release valve 6 opens by itself for processing. The pressure in the tank 2 is released to the atmospheric pressure. If desired, a steam trap or the like may be provided at the bottom of the processing tank 2.

減圧手段3は、処理槽2内の気体を外部へ吸引排出して、処理槽2内を減圧する。本実施例では、減圧手段3として、処理槽2内からの排気路7に、蒸気エゼクタ8、蒸気凝縮用の熱交換器9、逆止弁10、および水封式の真空ポンプ11を備える。 The depressurizing means 3 sucks and discharges the gas in the processing tank 2 to the outside to reduce the pressure in the processing tank 2. In this embodiment, as the depressurizing means 3, the exhaust passage 7 from the inside of the processing tank 2 is provided with a steam ejector 8, a heat exchanger 9 for steam condensation, a check valve 10, and a water-sealed vacuum pump 11.

蒸気エゼクタ8は、吸引口8aが処理槽2に接続されて設けられ、入口8bから出口8cへ向けて、エゼクタ給蒸路12からの蒸気がノズルで噴出可能とされる。入口8bから出口8cへ向けて蒸気を噴出させることで、処理槽2内の気体も吸引口8aを介して出口8cへ吸引排出される。エゼクタ給蒸路12に設けたエゼクタ給蒸弁13の開閉を操作することで、蒸気エゼクタ8の作動の有無を切り替えることができる。 The steam ejector 8 is provided with a suction port 8a connected to the processing tank 2, and steam from the ejector steam supply passage 12 can be ejected from the inlet 8b to the outlet 8c by a nozzle. By ejecting steam from the inlet 8b toward the outlet 8c, the gas in the processing tank 2 is also sucked and discharged to the outlet 8c through the suction port 8a. By operating the opening and closing of the ejector steaming valve 13 provided in the ejector steaming passage 12, it is possible to switch whether or not the steam ejector 8 is activated.

熱交換器9は、排気路7内の流体と冷却水とを混ぜることなく熱交換する間接熱交換器である。熱交換器9は、熱交給水路14を介して冷却水が供給され、熱交排水路15を介して冷却水が排出される。熱交給水路14には、熱交給水弁16と逆止弁17とが設けられている。熱交給水弁16を開けることで、熱交換器9に冷却水を通すことができる。熱交換器9に通水することで、熱交換器9において、排気路7内の蒸気を冷却水により冷却して凝縮させることができる。なお、熱交給水弁16は、熱交給水路14に設けられたが、場合により、熱交排水路15に設けられてもよい。 The heat exchanger 9 is an indirect heat exchanger that exchanges heat without mixing the fluid in the exhaust passage 7 with the cooling water. In the heat exchanger 9, the cooling water is supplied through the heat exchange water supply channel 14, and the cooling water is discharged through the heat exchange drainage channel 15. The heat exchange water supply channel 14 is provided with a heat exchange water supply valve 16 and a check valve 17. By opening the heat exchange water valve 16, cooling water can be passed through the heat exchanger 9. By passing water through the heat exchanger 9, the steam in the exhaust passage 7 can be cooled and condensed by the cooling water in the heat exchanger 9. The heat exchange water supply valve 16 is provided in the heat exchange water supply channel 14, but may be provided in the heat exchange drainage channel 15 as the case may be.

真空ポンプ11は、水封式であり、周知のとおり、封水と呼ばれる水が供給されつつ運転される。真空ポンプ11への封水給水路18には、封水給水弁19が設けられており、この封水給水弁19を開けることで、真空ポンプ11に封水を供給することができる。封水給水弁19の開閉は、真空ポンプ11の発停と連動する。封水給水弁19を開けた状態で真空ポンプ11を作動させると、真空ポンプ11は、熱交換器9の側から流体を吸引して排出する。 The vacuum pump 11 is a water-sealed type, and as is well known, the vacuum pump 11 is operated while being supplied with water called water-sealed. A water-sealing water supply valve 19 is provided in the water-sealing water supply channel 18 to the vacuum pump 11, and by opening the water-sealing water supply valve 19, the water-sealing water can be supplied to the vacuum pump 11. The opening and closing of the sealed water supply valve 19 is linked to the start and stop of the vacuum pump 11. When the vacuum pump 11 is operated with the sealed water supply valve 19 open, the vacuum pump 11 sucks fluid from the heat exchanger 9 side and discharges the fluid.

蒸気発生タンク4は、水を貯留する中空容器である。蒸気発生タンク4は、その形状を特に問わないが、本実施例では略円筒状に形成されている。この際、略円筒状の蒸気発生タンク4は、軸線を上下方向へ沿って配置され、上下の開口部は閉塞されている。 The steam generation tank 4 is a hollow container for storing water. The shape of the steam generation tank 4 is not particularly limited, but in this embodiment, it is formed in a substantially cylindrical shape. At this time, the substantially cylindrical steam generation tank 4 is arranged along the vertical direction along the axis, and the upper and lower openings are closed.

蒸気発生タンク4は、連通路20を介して、処理槽2と連通して設けられる。本実施例では、連通路20には弁は設けられず、蒸気発生タンク4内は処理槽2内と常時連通する。連通路20は、好ましくは、一端部が蒸気発生タンク4の上部に接続され、他端部が処理槽2の下方側部に接続される。 The steam generation tank 4 is provided so as to communicate with the processing tank 2 via the communication passage 20. In this embodiment, the communication passage 20 is not provided with a valve, and the inside of the steam generation tank 4 is always in communication with the inside of the processing tank 2. The communication passage 20 is preferably connected at one end to the upper part of the steam generating tank 4 and the other end to the lower side of the processing tank 2.

蒸気発生タンク4は、設定水位まで水が貯留され、その貯留水が加熱されることで、処理槽2内へ蒸気を供給可能とされる。そのために、蒸気発生タンク4には、タンク給水手段21、タンク排水手段22およびタンク給蒸手段23が設けられる。 Water is stored in the steam generation tank 4 up to a set water level, and the stored water is heated so that steam can be supplied into the treatment tank 2. Therefore, the steam generating tank 4 is provided with a tank water supply means 21, a tank drainage means 22, and a tank steaming means 23.

タンク給水手段21は、タンク給水路24を介して、蒸気発生タンク4に水を供給する。蒸気発生タンク4へのタンク給水路24には、タンク給水弁25が設けられる。タンク給水弁25を開けることで、蒸気発生タンク4に給水することができる。 The tank water supply means 21 supplies water to the steam generation tank 4 via the tank water supply channel 24. A tank water supply valve 25 is provided in the tank water supply channel 24 to the steam generation tank 4. By opening the tank water supply valve 25, water can be supplied to the steam generation tank 4.

タンク排水手段22は、タンク排水路26を介して、蒸気発生タンク4から水を排出する。蒸気発生タンク4からのタンク排水路26には、タンク排水弁27と逆止弁28とが順に設けられる。タンク排水弁27を開けることで、蒸気発生タンク4から排水することができる。 The tank drainage means 22 discharges water from the steam generation tank 4 via the tank drainage channel 26. A tank drain valve 27 and a check valve 28 are sequentially provided in the tank drainage channel 26 from the steam generation tank 4. By opening the tank drain valve 27, drainage can be performed from the steam generation tank 4.

本実施例では、タンク給水路24とタンク排水路26とは、蒸気発生タンク4の下部に接続される。タンク給水弁25よりも下流側(蒸気発生タンク4側)のタンク給水路24と、タンク排水弁27よりも上流側(蒸気発生タンク4側)のタンク排水路26とは、共通管路29とされている。 In this embodiment, the tank water supply channel 24 and the tank drainage channel 26 are connected to the lower part of the steam generation tank 4. The tank water supply channel 24 on the downstream side (steam generation tank 4 side) of the tank water supply valve 25 and the tank drainage channel 26 on the upstream side (steam generation tank 4 side) of the tank drainage valve 27 are the common pipeline 29. Has been done.

タンク給蒸手段23は、タンク給蒸路30を介して、蒸気発生タンク4内の貯留水中に蒸気(ボイラやリボイラからの蒸気)を吹き込んで、貯留水を加熱する。蒸気発生タンク4へのタンク給蒸路30には、給蒸遮断弁31とタンク給蒸弁32とが順に設けられている。給蒸遮断弁31は、開閉をオンオフで切り替えられる弁(たとえば電磁弁)であり、タンク給蒸弁32は、好ましくは、開度を調整可能な弁(たとえば比例制御弁)である。給蒸遮断弁31は、タンク給蒸弁32を開ける際、連動して開けられる。給蒸遮断弁31およびタンク給蒸弁32を開けることで、蒸気発生タンク4内の貯留水中に蒸気を供給することができる。その際、タンク給蒸弁32の開度を調整することで、蒸気発生タンク4内への蒸気供給量を調整することができる。なお、図示例では、蒸気発生タンク4内の上部には、蒸気の乾き度を向上するためのバッフル板33が設けられている。 The tank steaming means 23 blows steam (steam from a boiler or a reboiler) into the stored water in the steam generating tank 4 via the tank steaming passage 30 to heat the stored water. A steam supply shutoff valve 31 and a tank steam supply valve 32 are sequentially provided in the tank steam supply passage 30 to the steam generation tank 4. The steam supply shutoff valve 31 is a valve (for example, a solenoid valve) that can be switched on and off, and the tank steam supply valve 32 is preferably a valve whose opening degree can be adjusted (for example, a proportional control valve). The steam supply shutoff valve 31 is opened in conjunction with the opening of the tank steam supply valve 32. By opening the steam supply shutoff valve 31 and the tank steam supply valve 32, steam can be supplied to the stored water in the steam generation tank 4. At that time, by adjusting the opening degree of the tank steam supply valve 32, the amount of steam supplied into the steam generation tank 4 can be adjusted. In the illustrated example, a baffle plate 33 for improving the dryness of steam is provided in the upper part of the steam generation tank 4.

復圧手段5は、減圧された処理槽2内へ外気を導入して、処理槽2内を復圧する。本実施例では、復圧手段5として、処理槽2内への給気路34に、エアフィルタ35と真空解除弁36とを備える。処理槽2内が減圧された状態で、真空解除弁36を開けると、外気がエアフィルタ35を介して処理槽2内へ導入され、処理槽2内を復圧することができる。真空解除弁36は、好ましくは、開度調整可能な弁(たとえば比例制御弁)から構成される。 The depressurizing means 5 introduces outside air into the depressurized treatment tank 2 to repressurize the inside of the treatment tank 2. In this embodiment, the air filter 35 and the vacuum release valve 36 are provided in the air supply path 34 into the treatment tank 2 as the pressure reducing means 5. When the vacuum release valve 36 is opened while the inside of the treatment tank 2 is depressurized, the outside air is introduced into the treatment tank 2 via the air filter 35, and the inside of the treatment tank 2 can be recompressed. The vacuum release valve 36 is preferably composed of a valve whose opening degree can be adjusted (for example, a proportional control valve).

蒸気発生タンク4には、圧力センサ37が設けられる。本実施例では、圧力センサ37は、蒸気発生タンク4の上部に設けられて、気相部の圧力を検出する。但し、処理槽2と蒸気発生タンク4とは、連通路20で連通されているので、圧力センサ37は、蒸気発生タンク4ではなく処理槽2に設けられてもよい。あるいは、処理槽2または蒸気発生タンク4内の圧力を検出可能であれば、その他の箇所(たとえば連通路20)に設けられてもよい。 The steam generation tank 4 is provided with a pressure sensor 37. In this embodiment, the pressure sensor 37 is provided in the upper part of the steam generation tank 4 and detects the pressure in the gas phase portion. However, since the processing tank 2 and the steam generation tank 4 are communicated with each other by the communication passage 20, the pressure sensor 37 may be provided in the processing tank 2 instead of the steam generation tank 4. Alternatively, if the pressure in the processing tank 2 or the steam generation tank 4 can be detected, it may be provided in another place (for example, the communication passage 20).

蒸気発生タンク4には、タンク内の水位を検出する水位センサ38が設けられる。水位センサ38としては、本実施例では電極式水位検出器が用いられるが、これに限らず、たとえば静電容量式水位検出器などを用いることもできる。 The steam generation tank 4 is provided with a water level sensor 38 that detects the water level in the tank. As the water level sensor 38, an electrode type water level detector is used in this embodiment, but the water level sensor 38 is not limited to this, and for example, a capacitance type water level detector or the like can also be used.

制御手段は、前記各センサ37,38の検出信号や経過時間などに基づき、前記各手段3,5,21,22,23を制御する制御器(図示省略)である。具体的には、真空ポンプ11、エゼクタ給蒸弁13、熱交給水弁16、封水給水弁19、タンク給水弁25、タンク排水弁27、給蒸遮断弁31、タンク給蒸弁32、真空解除弁36の他、圧力センサ37および水位センサ38などは、制御器に接続されている。そして、制御器は、所定の手順(プログラム)に従い、処理槽2内の被解凍物の解凍を図る。典型的には、空気排除工程の後、解凍処理工程を含んで運転することで、処理槽2内の被解凍物の解凍を図る。以下、具体的な運転例について説明する。 The control means is a controller (not shown) that controls the means 3, 5, 21, 22, 23 based on the detection signals of the sensors 37, 38, the elapsed time, and the like. Specifically, a vacuum pump 11, an ejector steam supply valve 13, a heat exchange water supply valve 16, a sealed water supply valve 19, a tank water supply valve 25, a tank drain valve 27, a steam supply shutoff valve 31, a tank steam supply valve 32, and a vacuum. In addition to the release valve 36, the pressure sensor 37, the water level sensor 38, and the like are connected to the controller. Then, the controller attempts to thaw the object to be thawed in the processing tank 2 according to a predetermined procedure (program). Typically, after the air removal step, the operation including the thawing treatment step is performed to thaw the object to be thawed in the treatment tank 2. Hereinafter, a specific operation example will be described.

運転開始に先立ち、予め、処理槽2内には被解凍物が収容され、処理槽2の扉は気密に閉じられる。その際、真空解除弁36が開けられているが、その他の弁は閉じられており、真空ポンプ11は停止している。スタートボタンが押されるなど、運転開始が指示されると、制御器は、空気排除工程の後、解凍処理工程を実行する。 Prior to the start of operation, the object to be thawed is housed in the treatment tank 2 in advance, and the door of the treatment tank 2 is airtightly closed. At that time, the vacuum release valve 36 is opened, but the other valves are closed, and the vacuum pump 11 is stopped. When the start of operation is instructed, such as when the start button is pressed, the controller executes a thawing process after the air evacuating step.

また、遅くとも解凍処理工程の開始までに、蒸気発生タンク4には、タンク給水手段21により設定水位まで水が貯留される。以後、解凍処理工程の終了まで、水位センサ38の検出信号に基づきタンク給水手段21とタンク排水手段22とを制御することで、蒸気発生タンク4内の貯留水は設定水位(設定範囲)に維持される。 Further, at the latest, by the start of the thawing process, water is stored in the steam generation tank 4 up to the set water level by the tank water supply means 21. After that, by controlling the tank water supply means 21 and the tank drainage means 22 based on the detection signal of the water level sensor 38 until the end of the thawing process, the stored water in the steam generation tank 4 is maintained at the set water level (set range). Will be done.

なお、後述する第一設定圧力や第三設定圧力は、ある圧力範囲としてもよいし、ある所定圧力としてもよい。圧力範囲とする場合、その上限圧力と下限圧力との範囲に収めるように、処理槽2内の減圧や処理槽2内への給蒸が制御される。 The first set pressure and the third set pressure, which will be described later, may be set to a certain pressure range or a certain predetermined pressure. When the pressure range is set, the depressurization in the treatment tank 2 and the steam supply into the treatment tank 2 are controlled so as to be within the range of the upper limit pressure and the lower limit pressure.

空気排除工程では、真空解除弁36を閉じた状態で、減圧手段3により処理槽2内を第一設定圧力(たとえば8hPa)まで減圧する。但し、第一設定圧力まで減圧することに代えて、第一設定時間だけ減圧してもよい。いずれにしても、空気排除工程では、封水給水弁19を開けると共に真空ポンプ11を作動させて、処理槽2内を減圧する。また、減圧中、設定タイミング(典型的には所定圧力以下)になると、エゼクタ給蒸弁13を開けて蒸気エゼクタ8を作動させると共に、熱交給水弁16を開けて熱交換器9に冷却水を通す。処理槽2内を所定まで減圧すると、減圧手段3を停止して、次工程へ移行する。 In the air evacuating step, with the vacuum release valve 36 closed, the inside of the processing tank 2 is depressurized to the first set pressure (for example, 8 hPa) by the depressurizing means 3. However, instead of reducing the pressure to the first set pressure, the pressure may be reduced for the first set time. In any case, in the air exhausting step, the sealing water supply valve 19 is opened and the vacuum pump 11 is operated to reduce the pressure in the treatment tank 2. Further, during depressurization, when the set timing (typically, a predetermined pressure or less) is reached, the ejector steam supply valve 13 is opened to operate the steam ejector 8, and the heat exchange water supply valve 16 is opened to cool water to the heat exchanger 9. Through. When the pressure inside the processing tank 2 is reduced to a predetermined level, the pressure reducing means 3 is stopped and the process proceeds to the next step.

解凍処理工程では、タンク給蒸手段23により蒸気発生タンク4内の貯留水を加熱し、これにより発生させた蒸気を処理槽2内へ供給して、処理槽2内の被解凍物の解凍を図る。本実施例では、蒸気発生タンク4から処理槽2内への蒸気供給は、第二設定圧力(たとえば飽和温度が18~20℃相当の圧力)まで行われ、第二設定圧力にて第二設定時間保持する。すなわち、空気排除工程にて第一設定圧力まで減圧後、解凍処理工程において第二設定圧力まで蒸気で復圧して、第二設定圧力にて第二設定時間保持する。 In the thawing treatment step, the stored water in the steam generation tank 4 is heated by the tank steaming means 23, and the steam generated by the heating is supplied to the treatment tank 2 to thaw the defrosted material in the treatment tank 2. Try. In this embodiment, the steam supply from the steam generation tank 4 to the processing tank 2 is performed up to the second set pressure (for example, the saturation temperature is a pressure equivalent to 18 to 20 ° C.), and the second set pressure is set. Hold time. That is, after depressurizing to the first set pressure in the air exclusion step, the pressure is restored to the second set pressure in the thawing process step with steam, and the pressure is maintained at the second set pressure for the second set time.

具体的には、第二設定圧力に維持するように、圧力センサ37の検出圧力に基づきタンク給蒸弁32の開度を調整する。この間、減圧手段3を停止させたままでよいが、場合により、減圧手段3を作動させつつタンク給蒸弁32の開度を調整してもよい。あるいは、第二設定圧力の上限圧力までの蒸気供給と、蒸気供給を停止(タンク給蒸弁32を閉鎖)した状態での下限圧力までの蒸気凝縮(待機)とを繰り返してもよい。その他、第二設定圧力での保持中、減圧手段3を作動させて、処理槽2内を一時的に減圧してもよい。 Specifically, the opening degree of the tank steam supply valve 32 is adjusted based on the detected pressure of the pressure sensor 37 so as to maintain the second set pressure. During this period, the decompression means 3 may be kept stopped, but in some cases, the opening degree of the tank steam supply valve 32 may be adjusted while the decompression means 3 is operated. Alternatively, steam supply up to the upper limit pressure of the second set pressure and steam condensation (standby) up to the lower limit pressure in a state where the steam supply is stopped (the tank steam supply valve 32 is closed) may be repeated. In addition, the depressurizing means 3 may be operated during the holding at the second set pressure to temporarily depressurize the inside of the processing tank 2.

本処理として第二設定圧力で第二設定時間保持した後、所望により、シメ処理として、第二設定圧力よりも低い第三設定圧力(たとえば飽和温度が8℃相当の圧力)まで減圧して、第三設定時間保持してもよい。さらに、その後、低温保持処理として、処理槽2内の圧力および温度を、所定時間、所定の圧力および温度に保持してもよい。その際、その圧力および温度は、時間経過と共に徐々に高くなるように調整してもよい。シメ処理および低温保持処理は、制御目標温度が異なるが、前記本処理と同様の制御で実施することができる。 After holding at the second set pressure for the second set time as the main treatment, if desired, the pressure is reduced to a third set pressure lower than the second set pressure (for example, a pressure equivalent to a saturation temperature of 8 ° C.) as a squeezing treatment. The third set time may be held. Further, after that, as a low temperature holding process, the pressure and temperature in the treatment tank 2 may be held at a predetermined pressure and temperature for a predetermined time. At that time, the pressure and temperature may be adjusted so as to gradually increase with the passage of time. Although the control target temperature is different, the squeeze treatment and the low temperature holding treatment can be carried out under the same control as the main treatment.

一連の解凍処理工程を終了すると、減圧手段3を停止すると共に、蒸気発生タンク4での蒸気発生を停止した状態で、復圧手段5により処理槽2内を大気圧まで復圧する。これにより、処理槽2の扉をあけて、処理槽2内から被解凍物を取り出すことができる。 When the series of thawing processing steps is completed, the depressurizing means 3 is stopped, and the inside of the processing tank 2 is restored to the atmospheric pressure by the pressure reducing means 5 in a state where the steam generation in the steam generation tank 4 is stopped. As a result, the door of the processing tank 2 can be opened and the defrosted material can be taken out from the inside of the processing tank 2.

本実施例の真空解凍装置1によれば、蒸気発生タンク4内が処理槽2内と常時連通して設けられるので、空気排除工程において処理槽2内を減圧すると、蒸気発生タンク4内も同等圧力に減圧される。これに伴い、解凍処理工程において、蒸気発生タンク4では処理槽2内の圧力に応じた飽和蒸気が発生するため、その蒸気を処理槽2内へ供給しても、処理槽2内で過熱が生じるおそれがなく、所望温度でムラなく被解凍物を加熱することができる。すなわち、処理槽2内および蒸気発生タンク4内が同じ圧力下にある状態(言い換えれば蒸気発生タンク4内を処理槽2と同じく目標温度相当の真空度にした状態)で、タンク給蒸手段23により蒸気発生タンク4内の貯留水に蒸気を吹き込むと、吹き込まれた蒸気は貯留水に熱を伝えて飽和蒸気になると共に、貯留水は蒸気発生タンク4の圧力(処理槽2内の減圧)に応じた温度で減圧沸騰し飽和蒸気を発生する。これにより、蒸気の過熱を防止して、所望温度でムラなく被解凍物を加熱することができる。 According to the vacuum thawing device 1 of the present embodiment, the inside of the steam generation tank 4 is always in communication with the inside of the treatment tank 2, so that when the inside of the treatment tank 2 is depressurized in the air exhausting step, the inside of the steam generation tank 4 is also the same. The pressure is reduced. Along with this, in the thawing treatment step, saturated steam is generated in the steam generation tank 4 according to the pressure in the treatment tank 2, so that even if the steam is supplied into the treatment tank 2, overheating occurs in the treatment tank 2. The object to be thawed can be heated evenly at a desired temperature without any possibility of occurrence. That is, the tank steaming means 23 is in a state where the inside of the treatment tank 2 and the inside of the steam generation tank 4 are under the same pressure (in other words, the inside of the steam generation tank 4 has a vacuum degree equivalent to the target temperature like the treatment tank 2). When steam is blown into the stored water in the steam generation tank 4, the blown steam transfers heat to the stored water to become saturated steam, and the stored water is the pressure of the steam generation tank 4 (decompression in the treatment tank 2). It boils under reduced pressure at a temperature corresponding to the above temperature to generate saturated steam. This makes it possible to prevent the steam from overheating and evenly heat the object to be thawed at a desired temperature.

ところで、仮に、蒸気発生タンク4を設けずに、処理槽2内の底部に水を溜めてその貯留水を加熱して、被解凍物の解凍を図るとすれば、次のような不都合がある。すなわち、まず、被解凍物が収容される処理槽2内に水を溜めてその貯留水を減圧沸騰させるとすれば、突沸が生じた場合、貯留水の飛沫が被解凍物に付着するおそれがある。また、解凍処理工程では、被解凍物から油分やドリップなどが溶出する場合があるが、これらの溶出物により貯留水が汚れ、ヒータおよび貯水部への汚れの堆積や細菌汚染のリスクがある。さらに、仮に処理槽2内の底部に貯水部やヒータを設けた場合、処理槽2内の洗浄が困難となり、処理槽2内を衛生的に保つことが難しくなる。 By the way, if water is stored in the bottom of the treatment tank 2 and the stored water is heated to thaw the thawed material without providing the steam generation tank 4, there are the following inconveniences. .. That is, if water is first stored in the treatment tank 2 in which the defrosted material is stored and the stored water is boiled under reduced pressure, if sudden boiling occurs, droplets of the stored water may adhere to the defrosted material. be. Further, in the thawing treatment step, oil and drip may be eluted from the defrosted material, but these elutions may contaminate the stored water, and there is a risk of contamination on the heater and the water storage portion and bacterial contamination. Further, if a water storage unit or a heater is provided at the bottom of the treatment tank 2, it becomes difficult to clean the inside of the treatment tank 2 and it becomes difficult to keep the inside of the treatment tank 2 hygienic.

これに対し、前記実施例の真空解凍装置1によれば、処理槽2とは別に蒸気発生タンク4を設けると共に、好ましくは蒸気発生タンク4の上部にバッフル板33を設けることで、貯留水の飛沫の流出を防止することができる。また、処理槽2とは別に蒸気発生タンク4を設けることで、被解凍物の油分やドリップ等によって、貯留水や蒸気発生部が汚れるおそれもない。しかも、運転中の流体の流れは、蒸気発生タンク4から処理槽2内への一方通行となるので、貯留水や蒸気発生部の汚染は確実に防止される。さらに、蒸気発生タンク4は水位制御され貯水量は大きくないため、1バッチ毎に貯留水を入れ替えて、衛生的な運転を容易に実施することもできる。 On the other hand, according to the vacuum thawing device 1 of the above embodiment, the steam generation tank 4 is provided separately from the treatment tank 2, and the baffle plate 33 is preferably provided on the upper part of the steam generation tank 4, so that the stored water is stored. It is possible to prevent the outflow of droplets. Further, by providing the steam generation tank 4 separately from the treatment tank 2, there is no possibility that the stored water or the steam generation portion is contaminated by the oil content or drip of the object to be thawed. Moreover, since the flow of the fluid during operation is one-way from the steam generating tank 4 to the inside of the processing tank 2, contamination of the stored water and the steam generating portion is surely prevented. Further, since the steam generation tank 4 is controlled by the water level and the stored water amount is not large, the stored water can be replaced for each batch to easily carry out hygienic operation.

本発明の真空解凍装置1は、前記実施例の構成(制御を含む)に限らず、適宜変更可能である。特に、(a)被解凍物が収容される処理槽2と、(b)処理槽2内の気体を外部へ吸引排出して処理槽2内を減圧する減圧手段3と、(c)処理槽2内と連通して設けられ、貯留水が加熱されることで処理槽2内へ蒸気を供給可能な蒸気発生タンク4とを備えるのであれば、その他の構成は適宜に変更可能である。 The vacuum thawing device 1 of the present invention is not limited to the configuration (including control) of the above embodiment, and can be appropriately changed. In particular, (a) a treatment tank 2 in which an object to be thawed is housed, (b) a decompression means 3 for sucking and discharging the gas in the treatment tank 2 to the outside to reduce the pressure in the treatment tank 2, and (c) a treatment tank. Other configurations can be appropriately changed as long as the steam generating tank 4 is provided so as to communicate with the inside of the 2 and can supply steam into the treatment tank 2 by heating the stored water.

たとえば、前記実施例では、蒸気発生タンク4内の貯留水は、タンク給蒸手段23により蒸気が直接に吹き込まれることで加熱されたが、蒸気ヒータにより間接的に加熱されてもよい。蒸気ヒータを用いる場合、蒸気発生タンク4の貯留水中に蒸気管(たとえばコイル)を設置し、その蒸気管内へタンク給蒸手段23により蒸気を供給することで、貯留水を加熱する。この場合も、解凍処理工程では、圧力センサ37の検出圧力に基づき、タンク給蒸弁32の開度(または開閉)を制御すればよい。蒸気ヒータへ供給された蒸気の凝縮水は、蒸気トラップを介して外部へ排出される。 For example, in the above embodiment, the stored water in the steam generating tank 4 is heated by directly blowing steam by the tank steaming means 23, but may be indirectly heated by the steam heater. When a steam heater is used, a steam pipe (for example, a coil) is installed in the stored water of the steam generation tank 4, and steam is supplied into the steam pipe by the tank steaming means 23 to heat the stored water. In this case as well, in the thawing process, the opening degree (or opening / closing) of the tank steaming valve 32 may be controlled based on the detected pressure of the pressure sensor 37. The condensed water of steam supplied to the steam heater is discharged to the outside through the steam trap.

あるいは、タンク給蒸手段23の設置を省略する代わりに、電気ヒータを用いてもよい。電気ヒータを用いる場合、解凍処理工程では、圧力センサ37の検出圧力に基づき、電気ヒータの容量(または発停)を制御すればよい。蒸気ヒータまたは電気ヒータを用いる場合、蒸気発生タンク4内に蒸気が直接に吹き込まれないので、水位変動を抑えると共に、蒸気発生タンク4内の水質(ひいては処理槽2内への蒸気の質)を所望に維持しやすい。 Alternatively, an electric heater may be used instead of omitting the installation of the tank steaming means 23. When an electric heater is used, in the defrosting process, the capacity (or start / stop) of the electric heater may be controlled based on the detection pressure of the pressure sensor 37. When a steam heater or an electric heater is used, steam is not directly blown into the steam generation tank 4, so that the water level fluctuation is suppressed and the water quality in the steam generation tank 4 (and thus the quality of steam in the treatment tank 2) is improved. Easy to maintain as desired.

1 真空解凍装置
2 処理槽
3 減圧手段
4 蒸気発生タンク
5 復圧手段
6 加圧解除弁
7 排気路
8 蒸気エゼクタ(8a:吸引口、8b:入口、8c:出口)
9 熱交換器
10 逆止弁
11 真空ポンプ
12 エゼクタ給蒸路
13 エゼクタ給蒸弁
14 熱交給水路
15 熱交排水路
16 熱交給水弁
17 逆止弁
18 封水給水路
19 封水給水弁
20 連通路
21 タンク給水手段
22 タンク排水手段
23 タンク給蒸手段
24 タンク給水路
25 タンク給水弁
26 タンク排水路
27 タンク排水弁
28 逆止弁
29 共通管路
30 タンク給蒸路
31 給蒸遮断弁
32 タンク給蒸弁
33 バッフル板
34 給気路
35 エアフィルタ
36 真空解除弁
37 圧力センサ
38 水位センサ
1 Vacuum defroster 2 Processing tank 3 Decompression means 4 Steam generation tank 5 Depressurization means 6 Pressurization release valve 7 Exhaust passage 8 Steam ejector (8a: suction port, 8b: inlet, 8c: outlet)
9 Heat exchanger 10 Check valve 11 Vacuum pump 12 Ejector steam supply channel 13 Ejector steam supply valve 14 Heat exchange water supply channel 15 Heat exchange drainage channel 16 Heat exchange water supply valve 17 Check valve 18 Sealed water supply channel 19 Sealed water supply valve 20 consecutive passages 21 tank water supply means 22 tank drainage means 23 tank steam supply means 24 tank water supply channel 25 tank water supply valve 26 tank drainage channel 27 tank drain valve 28 check valve 29 common pipeline 30 tank steam supply channel 31 steam supply shutoff valve 32 Tank steam supply valve 33 Baffle plate 34 Air supply passage 35 Air filter 36 Vacuum release valve 37 Pressure sensor 38 Water level sensor

Claims (3)

被解凍物が収容される処理槽と、
前記処理槽内の気体を外部へ吸引排出して前記処理槽内を減圧する減圧手段と、
前記処理槽内と連通して設けられ、前記処理槽を介して前記減圧手段に接続され、貯留水が加熱されることで前記処理槽内へ蒸気を供給可能な蒸気発生タンクとを備え
前記蒸気発生タンク内の圧力に基づき、前記減圧手段による減圧と、前記蒸気発生タンクでの蒸気発生とを制御する
ことを特徴とする真空解凍装置。
A processing tank that houses the material to be thawed,
A decompression means for sucking and discharging the gas in the treatment tank to the outside to reduce the pressure in the treatment tank.
It is provided with a steam generation tank that is provided in communication with the inside of the treatment tank, is connected to the decompression means via the treatment tank, and can supply steam into the treatment tank by heating the stored water.
Based on the pressure in the steam generation tank, the depressurization by the depressurizing means and the steam generation in the steam generation tank are controlled.
A vacuum defroster characterized by that.
前記蒸気発生タンクは、貯留水中に蒸気が吹き込まれることで蒸気を発生させる
ことを特徴とする請求項1に記載の真空解凍装置。
The vacuum defrosting device according to claim 1, wherein the steam generation tank generates steam by blowing steam into the stored water.
前記蒸気発生タンクは、貯留水がヒータで加熱されることで蒸気を発生させる
ことを特徴とする請求項1に記載の真空解凍装置。
The vacuum defrosting device according to claim 1, wherein the steam generation tank generates steam by heating stored water with a heater.
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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009178106A (en) 2008-01-31 2009-08-13 Miura Co Ltd Thermal treatment equipment

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5486672A (en) * 1977-12-22 1979-07-10 Hitachi Plant Eng & Constr Co Defreezing apparatus for frozen food
JPS58205483A (en) * 1982-05-26 1983-11-30 Toshiba Corp Thawing apparatus
JPH0515358A (en) * 1991-07-04 1993-01-26 Hoshizaki Electric Co Ltd Vacuum defrosting apparatus

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009178106A (en) 2008-01-31 2009-08-13 Miura Co Ltd Thermal treatment equipment

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