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JP2007268017A - Steam-heating apparatus - Google Patents

Steam-heating apparatus Download PDF

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Publication number
JP2007268017A
JP2007268017A JP2006098421A JP2006098421A JP2007268017A JP 2007268017 A JP2007268017 A JP 2007268017A JP 2006098421 A JP2006098421 A JP 2006098421A JP 2006098421 A JP2006098421 A JP 2006098421A JP 2007268017 A JP2007268017 A JP 2007268017A
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Prior art keywords
steam
valve
steam supply
processing tank
temperature
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Japanese (ja)
Inventor
Akira Wakasa
暁 若狭
Katsutoshi Matsunaga
勝利 松永
Taizo Matsukawa
泰三 松川
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Miura Co Ltd
Miura Protec Co Ltd
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Miura Co Ltd
Miura Protec Co Ltd
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Priority to JP2006098421A priority Critical patent/JP2007268017A/en
Publication of JP2007268017A publication Critical patent/JP2007268017A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To prevent air retained in a reboiler and a steam supply pipe from being supplied to a processing tank when supplying steam to the processing tank. <P>SOLUTION: This steam-heating apparatus is provided with the processing tank 2 for storing a heated object 1, the reboiler 14 vaporizing soft water using the steam from a boiler 13 as a heat source, the steam supply pipe 22 supplying the steam from the reboiler 14 to the interior of the processing tank 2, a steam supply valve 24 provided in the steam supply pipe 22 and opening/closing the pipe line, and an exhaust valve 25 disposed adjacent to the steam supply valve 24 in the side of the boiler 14 of the steam supply valve 24. The exhaust valve 25 has an opening communicating between the inside/outside of the seam supply pipe 22 and closes the opening based on the temperature of the steam from the reboiler 14. A temperature regulation trap operated at a temperature lower than a saturated steam temperature by a prescribed temperature under the pressure of an installation place is used as the exhaust valve 25. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、被加熱物が収容された処理槽内へ蒸気を供給して、前記被加熱物を加熱するための蒸気加熱装置に関するものである。特に、被調理物(食材または食品)を加熱調理するための飽和蒸気調理装置などの蒸気加熱装置に関するものである。   The present invention relates to a steam heating apparatus for supplying steam into a treatment tank in which an object to be heated is accommodated to heat the object to be heated. In particular, the present invention relates to a steam heating device such as a saturated steam cooking device for cooking food to be cooked (food or food).

下記特許文献1に開示されるように、食材が収容された処理槽内へ蒸気を供給して、食材の加熱調理を図る蒸気加熱装置が知られている。この蒸気加熱装置では、予め処理槽内の空気を排出した後、処理槽内へ蒸気を供給することが、伝熱効率を高める上で好ましい。また、下記特許文献2に開示されるように、リボイラを用いて軟水を蒸気化し、その蒸気を処理槽内へ供給することが、安全で衛生的な調理を行う上で好ましい。
特開2005−210959号公報 (段落番号0037−0038、図1) 特開2005−65798号公報 (段落番号0018−0019、図1)
As disclosed in Patent Document 1 below, a steam heating apparatus is known in which steam is supplied into a treatment tank in which a food is stored, and the food is cooked. In this steam heating device, it is preferable to supply steam into the processing tank after exhausting the air in the processing tank in advance in order to increase the heat transfer efficiency. Further, as disclosed in Patent Document 2 below, it is preferable to vaporize soft water using a reboiler and supply the steam into the treatment tank in order to perform safe and hygienic cooking.
JP 2005-210959 A (paragraph numbers 0037-0038, FIG. 1) Japanese Patent Laying-Open No. 2005-65798 (paragraph numbers 0018-0019, FIG. 1)

しかしながら、処理槽内への蒸気を発生させるリボイラ内や、このリボイラからの蒸気を処理槽内へ供給する給蒸管内に溜まった空気が、前記給蒸管に設けた給蒸弁を開いて処理槽内へ蒸気供給する際に、処理槽内へ供給されてしまう不都合があった。そのため、せっかく予め処理槽内の空気を排除しておいても、処理槽内への蒸気供給初期に、処理槽内へ空気が導入されてしまい、空気排除の効果が減少または消滅するおそれがあった。   However, the air accumulated in the reboiler that generates steam into the treatment tank and in the steam supply pipe that supplies the steam from the reboiler into the treatment tank opens the steam supply valve provided in the steam supply pipe for treatment. When supplying steam into the tank, there was a problem of being supplied into the processing tank. For this reason, even if the air in the treatment tank is eliminated in advance, air may be introduced into the treatment tank at the initial stage of supplying steam to the treatment tank, and the effect of the air removal may be reduced or eliminated. It was.

一方、リボイラにおいても、リボイラ起動時にリボイラ内に空気が溜まったままであると、空気分圧の分だけ蒸気温度が低い状態となり、処理槽内への蒸気供給初期に、処理槽内への蒸気供給が円滑になされないおそれがあった。   On the other hand, in the reboiler, if the air remains in the reboiler when the reboiler is activated, the steam temperature is lowered by the amount of the partial pressure of the air. There was a risk that this could not be done smoothly.

本発明が解決しようとする課題は、処理槽内への蒸気供給時に、給蒸弁より上流側に溜まっていた空気が、処理槽内へ供給されてしまうのを防止することにある。また、リボイラ内に溜まっていた空気を排除することで、リボイラの起動を所望どおり行うことにある。   The problem to be solved by the present invention is to prevent air that has accumulated on the upstream side of the steam supply valve from being supplied into the processing tank when the steam is supplied into the processing tank. Further, the reboiler is started as desired by removing the air accumulated in the reboiler.

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、被加熱物が収容される処理槽と、この処理槽内へ蒸気発生装置からの蒸気を供給する給蒸管と、この給蒸管に設けられ、その管路を開閉する給蒸弁と、この給蒸弁より前記蒸気発生装置側の前記給蒸管に設けられ、設定温度未満では前記給蒸管の内外を連通するよう開口する一方、設定温度以上では前記開口を閉鎖する排気弁とを備えることを特徴とする蒸気加熱装置である。   The present invention has been made to solve the above-mentioned problems, and the invention according to claim 1 supplies a steam from a steam generator into a processing tank in which an object to be heated is accommodated, and the processing tank. A steam supply pipe, a steam supply valve provided in the steam supply pipe for opening and closing the conduit, and provided in the steam supply pipe on the steam generator side from the steam supply valve, and at a temperature lower than a set temperature, the steam supply pipe The steam heating apparatus includes an exhaust valve that opens to communicate the inside and outside of the pipe, and closes the opening at a set temperature or higher.

請求項1に記載の発明によれば、蒸気発生装置の起動時など、蒸気発生装置や給蒸管内に空気が溜まっている状態では、排気弁は開口している。従って、その溜まっていた空気は、蒸気発生装置からの蒸気により、排気弁を介して外部へ押し出され排出される。ところが、蒸気発生装置からの蒸気は、前記空気よりも高温であるため、空気排出後は排気弁の開口は閉じられる。従って、その後、給蒸管に設けた給蒸弁を開くことで、処理槽内へ蒸気のみを供給することができる。   According to the first aspect of the present invention, the exhaust valve is open when air is accumulated in the steam generator or the steam supply pipe, such as when the steam generator is started. Therefore, the accumulated air is pushed out to the outside through the exhaust valve by the steam from the steam generator and discharged. However, since the steam from the steam generator is hotter than the air, the opening of the exhaust valve is closed after the air is discharged. Therefore, after that, only the steam can be supplied into the treatment tank by opening the steam supply valve provided in the steam supply pipe.

請求項2に記載の発明は、前記処理槽内の空気を外部へ吸引排出する減圧手段と、前記蒸気発生装置内の蒸気圧を検出する蒸気圧検出手段と、この蒸気圧検出手段の検出信号に基づき前記給蒸弁の開閉を制御する制御手段とをさらに備えることを特徴とする請求項1に記載の蒸気加熱装置である。   According to a second aspect of the present invention, there is provided a decompression unit that sucks and discharges the air in the processing tank to the outside, a vapor pressure detection unit that detects a vapor pressure in the steam generator, and a detection signal of the vapor pressure detection unit The steam heating apparatus according to claim 1, further comprising: a control unit that controls opening and closing of the steam supply valve based on the above.

請求項2に記載の発明によれば、給蒸弁より下流側の給蒸管内の空気や、処理槽内の空気は、減圧手段により外部へ排出することができる。一方、上述したように、給蒸弁より上流側の給蒸管内の空気や、蒸気発生装置内の空気は、排気弁から外部へ排出することができる。このようにして、処理槽内の空気を排除すると共に、処理槽内へ空気を導入することなく、処理槽内へ蒸気を供給することができる。また、蒸気圧検出手段により、蒸気発生装置内の蒸気圧を所望にしてから、給蒸弁を開いて処理槽内へ蒸気を供給することができる。   According to invention of Claim 2, the air in the steam supply pipe | tube downstream from a steam supply valve and the air in a processing tank can be discharged | emitted outside by a pressure reduction means. On the other hand, as described above, the air in the steam supply pipe upstream of the steam supply valve and the air in the steam generator can be discharged from the exhaust valve to the outside. In this manner, it is possible to supply steam into the treatment tank without removing air in the treatment tank and introducing air into the treatment tank. Further, the steam pressure detection means can make the steam pressure in the steam generator desired, and then supply steam into the treatment tank by opening the steam supply valve.

請求項3に記載の発明は、被加熱物が収容される処理槽と、ボイラからの蒸気を熱源として軟水または純水を蒸気とするリボイラと、このリボイラからの蒸気を前記処理槽内へ供給する給蒸管と、この給蒸管に設けられ、その管路を開閉する給蒸弁と、この給蒸弁より前記リボイラ側に配置されると共に、前記給蒸弁に近接して前記給蒸管に設けられ、前記給蒸管の内外を連通する開口を有し、前記リボイラからの蒸気の温度に基づき前記開口を閉鎖する排気弁と、前記処理槽内の空気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、前記リボイラ内の蒸気圧を検出する蒸気圧検出手段と、この蒸気圧検出手段の検出信号に基づき、前記ボイラから前記リボイラへの蒸気供給と、前記給蒸弁の開閉の可否とを制御する制御手段とを備えることを特徴とする蒸気加熱装置である。   The invention according to claim 3 is a treatment tank in which an object to be heated is accommodated, a reboiler using steam from the boiler as heat source and soft water or pure water as steam, and supplying steam from the reboiler into the treatment tank. A steam supply pipe, a steam supply valve provided on the steam supply pipe for opening and closing the pipe, and disposed on the reboiler side from the steam supply valve, and in the vicinity of the steam supply valve, the steam supply pipe An exhaust valve that is provided in a pipe and has an opening that communicates the inside and outside of the steam supply pipe, closes the opening based on the temperature of the steam from the reboiler, and sucks and discharges the air in the processing tank to the outside. A decompression means for decompressing the inside of the treatment tank, a steam pressure detection means for detecting the steam pressure in the reboiler, a steam supply from the boiler to the reboiler based on a detection signal of the steam pressure detection means, Control means for controlling whether or not the steam supply valve can be opened and closed; A steam heating apparatus, characterized in that it comprises.

請求項3に記載の発明によれば、リボイラの起動時など、リボイラや給蒸管内に空気が溜まっている状態では、排気弁は開口している。従って、その溜まっていた空気は、リボイラからの蒸気により、排気弁を介して外部へ押し出され排出される。ところが、リボイラからの蒸気は、前記空気よりも高温であるため、空気排出後は排気弁の開口は閉じられる。従って、その後、給蒸管に設けた給蒸弁を開くことで、処理槽内へ蒸気のみを供給することができる。ここで、予め、給蒸弁より下流側の給蒸管内の空気や、処理槽内の空気は、減圧手段により外部へ排出しておくことができる。このようにして、処理槽内の空気を排除すると共に、処理槽内へ空気を導入することなく、処理槽内へ蒸気を供給することができる。また、蒸気圧検出手段に基づきボイラからリボイラへの蒸気供給を制御して、リボイラ内の蒸気圧を所望に維持しつつ、給蒸弁を開いて処理槽内へ蒸気を供給することができる。しかも、処理槽内へ供給される蒸気は、軟水または純水を蒸気化したものであるから、安全で衛生的な加熱処理が可能である。   According to the third aspect of the present invention, the exhaust valve is open in a state where air is accumulated in the reboiler or the steam supply pipe, such as when the reboiler is activated. Therefore, the accumulated air is pushed out by the steam from the reboiler and exhausted through the exhaust valve. However, since the steam from the reboiler is hotter than the air, the opening of the exhaust valve is closed after the air is discharged. Therefore, after that, only the steam can be supplied into the treatment tank by opening the steam supply valve provided in the steam supply pipe. Here, the air in the steam supply pipe on the downstream side of the steam supply valve and the air in the treatment tank can be discharged to the outside beforehand by the decompression means. In this manner, it is possible to supply steam into the treatment tank without removing air in the treatment tank and introducing air into the treatment tank. Further, the steam supply from the boiler to the reboiler is controlled based on the steam pressure detecting means, and the steam can be supplied into the treatment tank by opening the steam supply valve while maintaining the steam pressure in the reboiler as desired. Moreover, since the steam supplied into the treatment tank is obtained by vaporizing soft water or pure water, safe and sanitary heat treatment is possible.

請求項4に記載の発明は、前記排気弁は、設置箇所の圧力下における飽和蒸気温度より所定温度低い温度で作動する温調トラップとされたことを特徴とする請求項1〜3のいずれか1項に記載の蒸気加熱装置である。   The invention according to claim 4 is characterized in that the exhaust valve is a temperature control trap that operates at a temperature lower than the saturated steam temperature under the pressure of the installation location by a predetermined temperature. 2. A steam heating apparatus according to item 1.

請求項4に記載の発明によれば、温調トラップを用いることで、機械的に簡易に構成することができる。   According to invention of Claim 4, it can be comprised mechanically simply by using a temperature control trap.

さらに、請求項5に記載の発明は、前記排気弁は、前記給蒸弁より上流側の前記給蒸管内の温度を検出する管内温度検出手段の検出信号に基づき、設定温度以上で閉鎖するよう制御される開閉弁とされたことを特徴とする請求項1〜3のいずれか1項に記載の蒸気加熱装置である。   Furthermore, the invention according to claim 5 is such that the exhaust valve closes at a set temperature or higher based on a detection signal of a pipe temperature detecting means for detecting the temperature in the steam supply pipe upstream of the steam supply valve. It is set as the on-off valve controlled, It is a steam heating apparatus of any one of Claims 1-3 characterized by the above-mentioned.

請求項5に記載の発明によれば、管内温度検出手段と開閉弁とを用いて、電気的制御を用いて簡易に構成することができる。   According to invention of Claim 5, it can comprise simply using an electrical control using an in-pipe temperature detection means and an on-off valve.

本発明の蒸気加熱装置によれば、処理槽内への蒸気供給時に、給蒸弁より上流側に溜まっていた空気が、処理槽内へ供給されてしまうのを防止することができる。従って、処理槽内において、被加熱物の蒸気による加熱を、空気で阻害されることなく効率的に行うことができる。また、リボイラ内に溜まっていた空気を排除することで、リボイラの起動を所望どおりに行うことができる。   According to the steam heating apparatus of the present invention, it is possible to prevent air that has accumulated on the upstream side of the steam supply valve from being supplied into the processing tank when supplying steam into the processing tank. Therefore, in the treatment tank, heating of the object to be heated with steam can be efficiently performed without being inhibited by air. Further, by removing the air accumulated in the reboiler, the reboiler can be started as desired.

つぎに、本発明の実施の形態について説明する。
本発明は、処理槽内に収容された被加熱物を、蒸気により加熱する蒸気加熱装置である。ここで、被加熱物の種類は、特に問わないが、典型的には食材または食品などの被調理物とされる。この場合、蒸気加熱装置は、蒸気で被調理物を蒸したり煮たりする蒸煮機もしくは蒸し庫または飽和蒸気調理装置ということができる。また、蒸気による加熱調理後に、処理槽内の空気を外部へ吸引排出して、被調理物の真空冷却を図る場合には、蒸煮冷却機ということができる。あるいは、被加熱物は、手術用メスなどの被滅菌物でもよい。この場合、蒸気加熱装置は、蒸気滅菌装置ということができる。但し、本発明は、ここに例示した装置に限らず、空気排除後の処理槽内へ蒸気供給するその他の装置にも適用可能である。
Next, an embodiment of the present invention will be described.
The present invention is a steam heating apparatus that heats an object to be heated contained in a treatment tank with steam. Here, the type of the object to be heated is not particularly limited, but is typically an object to be cooked such as food or food. In this case, the steam heating device can be referred to as a steaming machine, a steamer, or a saturated steam cooking device that steams or boiles an object to be cooked with steam. In addition, after cooking by steam, when the air in the processing tank is sucked and discharged to the outside and the object to be cooked is vacuum-cooled, it can be called a steaming cooler. Alternatively, the object to be heated may be an object to be sterilized such as a surgical knife. In this case, the steam heating device can be referred to as a steam sterilization device. However, the present invention is not limited to the apparatus exemplified here, but can be applied to other apparatuses that supply steam into the treatment tank after the air is exhausted.

本実施形態の蒸気加熱装置は、被加熱物が収容される処理槽と、この処理槽内へ蒸気供給する給蒸手段と、処理槽内の気体を外部へ吸引排出して処理槽内を減圧する減圧手段と、減圧された処理槽内へ外気を導入して処理槽内を復圧する復圧手段と、処理槽内の蒸気やその凝縮水を外部へ排出する排出手段とを備える。   The steam heating apparatus of this embodiment includes a processing tank in which an object to be heated is stored, a steam supply means for supplying steam into the processing tank, and a vacuum in the processing tank by sucking and discharging the gas in the processing tank to the outside. Pressure reducing means, a decompression means for introducing outside air into the decompressed processing tank to restore the pressure in the processing tank, and a discharging means for discharging the steam in the processing tank and its condensed water to the outside.

前記処理槽は、被加熱物を収容可能な中空構造に形成され、典型的には略矩形のボックス状に形成された金属製の缶体である。この処理槽は、一側面へ開口して中空部を有する処理槽本体と、この処理槽本体の開口部を開閉する扉とから構成される。この扉が閉められた状態では、前記中空部は密閉される。但し、処理槽の構成はこれに限らず、上方へ開口する有底円筒状の処理槽本体と、この上部開口部を開閉可能に閉じる扉とから構成してもよい。   The said processing tank is a metal can body formed in the hollow structure which can accommodate a to-be-heated material, and was typically formed in the substantially rectangular box shape. This processing tank is comprised from the processing tank main body which opens to one side and has a hollow part, and the door which opens and closes the opening part of this processing tank main body. In a state where the door is closed, the hollow portion is sealed. However, the configuration of the processing tank is not limited to this, and may be configured from a bottomed cylindrical processing tank main body that opens upward, and a door that closes the upper opening so as to be openable and closable.

処理槽には、処理槽内の圧力を検出する圧力センサが設けられる。但し、処理槽内の圧力は温度と所定の関係にあるから、圧力センサに代えて、処理槽内の温度を検出する温度センサを用いてもよい。その他、処理槽には、処理槽内に収容される被加熱物の温度を検出する品温センサを設置してもよい。   The processing tank is provided with a pressure sensor that detects the pressure in the processing tank. However, since the pressure in the processing tank has a predetermined relationship with the temperature, a temperature sensor that detects the temperature in the processing tank may be used instead of the pressure sensor. In addition, you may install the product temperature sensor which detects the temperature of the to-be-heated material accommodated in a processing tank in a processing tank.

前記給蒸手段は、処理槽内へ蒸気発生装置からの蒸気を供給する手段である。蒸気発生装置は、典型的にはボイラから構成される。この際、ボイラ(一次ボイラ)からの蒸気を熱源として、軟水または純水をリボイラ(二次ボイラ)にて蒸気化し、このリボイラからの清浄蒸気を処理槽内へ供給するのが好ましい。これにより、配管内の錆や、防錆剤などのボイラ水処理薬品が、処理槽内への蒸気に混入されるおそれがなく衛生的である。以下の説明においては、蒸気発生装置はリボイラとして説明するが、単なるボイラであっても同様である。   The steam supply means is means for supplying steam from the steam generator into the treatment tank. The steam generator is typically composed of a boiler. At this time, it is preferable to vaporize soft water or pure water in a reboiler (secondary boiler) using steam from the boiler (primary boiler) as a heat source, and supply clean steam from the reboiler into the treatment tank. Thereby, boiler water treatment chemicals such as rust in the pipe and rust preventive agent are not sanitized and are hygienic. In the following description, the steam generator is described as a reboiler, but the same applies to a simple boiler.

蒸気発生装置としてのリボイラからの蒸気は、給蒸管を介して処理槽内へ供給される。この給蒸管の中途には、給蒸弁が開閉可能に設けられる。この給蒸弁を開閉することで、処理槽内への蒸気供給の有無が切り替えられる。この給蒸弁は、電磁弁のように全開または全閉のみ可能な構成でもよいし、モータバルブや比例制御弁のように開度調整可能な構成でもよい。   Steam from a reboiler as a steam generator is supplied into the treatment tank through a steam supply pipe. In the middle of the steam supply pipe, a steam supply valve is provided to be openable and closable. By opening and closing this steam supply valve, the presence or absence of steam supply into the treatment tank is switched. The steam supply valve may be configured to be fully open or fully closed like an electromagnetic valve, or may be configured to be adjustable in opening degree such as a motor valve or a proportional control valve.

さらに、給蒸管には、排気弁が設けられる。この排気弁は、給蒸管の外周壁を介して給蒸管の内外を連通するよう開口するが、リボイラからの蒸気の温度に基づき、その開口を閉鎖する構成である。すなわち、排気弁は、設定温度未満では給蒸管の内外を連通するよう開口する一方、設定温度以上では前記開口を閉鎖するよう構成される。このような排気弁は、給蒸弁よりリボイラ側に配置されるが、給蒸弁に近接した位置に設けるのが好ましい。また、給蒸管内に蒸気が流れている際に、その蒸気の温度を低下させずに検知可能に設置するのが好ましい。   Further, the steam supply pipe is provided with an exhaust valve. This exhaust valve opens so as to communicate the inside and outside of the steam supply pipe via the outer peripheral wall of the steam supply pipe, and is configured to close the opening based on the temperature of the steam from the reboiler. That is, the exhaust valve is configured to open so as to communicate with the inside and outside of the steam supply pipe when the temperature is lower than the set temperature, and closes the opening when the temperature is equal to or higher than the set temperature. Such an exhaust valve is disposed on the reboiler side of the steam supply valve, but is preferably provided at a position close to the steam supply valve. In addition, when steam is flowing in the steam supply pipe, it is preferable that the steam is installed so as to be detectable without lowering the temperature of the steam.

排気弁としては、典型的には温調トラップが用いられる。この温調トラップは、設置箇所の圧力下における飽和蒸気温度より所定温度低い温度で作動して、開口を閉じる構成である。本発明の場合、リボイラ起動時は大気圧下であり、その飽和蒸気温度は100℃であるから、そこからたとえば数℃から十数℃の範囲で選択された所定温度だけ低い温度(たとえば95℃)で、開口を閉鎖するよう作動する温調トラップが用いられる。この場合、給蒸管内に空気が残っている状態では、排気弁は開口しており、リボイラからの蒸気にて空気が外部へ押し出されて排出された後は、蒸気の温度に基づき閉鎖状態を維持する。このような温調トラップは、給蒸管の外周壁に直付けするなどして、給蒸管内を流れる蒸気の温度を低下させずに検出可能に設置するのが好ましい。この際、給蒸管の水平配管部の上周面に設置すれば、ドレンの排出を防止して、空気のみを排出させることができる。   A temperature control trap is typically used as the exhaust valve. This temperature control trap is configured to operate at a predetermined temperature lower than the saturated steam temperature under the pressure of the installation location and close the opening. In the case of the present invention, when the reboiler is started, it is under atmospheric pressure, and its saturated steam temperature is 100 ° C., so that the temperature is lower by a predetermined temperature selected from a range of several to tens of degrees C (for example, 95 ° C.). ), A temperature control trap that operates to close the opening is used. In this case, when the air remains in the steam supply pipe, the exhaust valve is open, and after the air is pushed out by the steam from the reboiler and discharged, the exhaust valve is closed based on the temperature of the steam. maintain. Such a temperature control trap is preferably installed so as to be detectable without lowering the temperature of the steam flowing in the steam supply pipe, for example, by directly attaching to the outer peripheral wall of the steam supply pipe. At this time, if it is installed on the upper peripheral surface of the horizontal pipe section of the steam supply pipe, drainage can be prevented and only air can be discharged.

但し、排気弁として、温調トラップに代えて、電磁弁などの開閉弁を、管内温度検出手段としての温度センサと共に用いてもよい。この場合、給蒸管の中途部には、前記給蒸弁と近接した位置に、短い分岐管を接続し、この分岐管に開閉弁を配置する。分岐管は、その先端が開口されており、開閉弁を開いた状態では、給蒸管の内外が連通される。そして、この開閉弁は、給蒸弁より上流側の給蒸管内に設けた温度センサの検出信号に基づき、開閉制御される。すなわち、設定温度未満の場合には、前記開閉弁を開口する一方、設定温度以上の場合には前記開閉弁を閉鎖する。   However, an open / close valve such as a solenoid valve may be used as an exhaust valve together with a temperature sensor as a pipe temperature detecting means instead of the temperature control trap. In this case, a short branch pipe is connected to the middle portion of the steam supply pipe at a position close to the steam supply valve, and an open / close valve is disposed in the branch pipe. The branch pipe has an open end, and the inside and outside of the steam supply pipe communicate with each other when the on-off valve is opened. The opening / closing valve is controlled to open / close based on a detection signal of a temperature sensor provided in the steam supply pipe upstream of the steam supply valve. That is, when the temperature is lower than the set temperature, the on-off valve is opened, and when the temperature is higher than the set temperature, the on-off valve is closed.

前記減圧手段は、処理槽内の気体(空気および/または蒸気)を外部へ吸引排出して、処理槽内を減圧する手段である。この減圧手段は、真空ポンプ、蒸気エゼクタまたは水エゼクタなどを備える。これらは、いずれか単独で用いてもよいし、複数個または複数種のものを組み合わせてもよい。このような減圧手段を作動させることで、処理槽の気体は排気管を介して外部へ吸引排出され、処理槽内の減圧が図られる。処理槽内の減圧の有無は、減圧手段の作動の有無を切り替えることでなされる。あるいは、排気管の中途に真空弁を設け、その開閉を操作してもよい。   The decompression means is means for decompressing the inside of the processing tank by sucking and discharging the gas (air and / or vapor) in the processing tank to the outside. The decompression means includes a vacuum pump, a steam ejector, a water ejector, or the like. Any of these may be used alone, or a plurality of them may be used in combination. By operating such a pressure reducing means, the gas in the processing tank is sucked and discharged to the outside through the exhaust pipe, and the pressure in the processing tank is reduced. The presence or absence of decompression in the treatment tank is made by switching the presence or absence of the operation of the decompression means. Alternatively, a vacuum valve may be provided in the middle of the exhaust pipe and its opening / closing may be operated.

減圧手段として蒸気エゼクタを用いる場合、排気管には蒸気エゼクタより下流側に、凝縮器としての熱交換器が通常備えられる。また、減圧手段として真空ポンプを用いる場合、排気管には真空ポンプより上流側に、凝縮器としての熱交換器を備えるのが望ましい。ここで、熱交換器は、排気管内の蒸気を冷却し凝縮させる凝縮器である。この冷却および凝縮作用をなすために、熱交換器には冷却用水が供給され、排気管の冷却が図られる。熱交換器の下流側に真空ポンプが配置される場合、排気管中の蒸気を予め熱交換器で凝縮させておくことで、その後の真空ポンプの負荷を軽減して、減圧能力を高めることができる。   When a steam ejector is used as the decompression means, the exhaust pipe is usually provided with a heat exchanger as a condenser downstream of the steam ejector. When a vacuum pump is used as the decompression means, it is desirable that the exhaust pipe is provided with a heat exchanger as a condenser upstream of the vacuum pump. Here, the heat exchanger is a condenser that cools and condenses the steam in the exhaust pipe. In order to perform this cooling and condensation action, cooling water is supplied to the heat exchanger, and the exhaust pipe is cooled. When a vacuum pump is arranged on the downstream side of the heat exchanger, the steam in the exhaust pipe is condensed in advance with the heat exchanger, thereby reducing the load on the subsequent vacuum pump and increasing the decompression capacity. it can.

前記復圧手段は、減圧手段により減圧された処理槽内へ外気を導入して、処理槽内を復圧する手段である。処理槽内への外気の導入は、衛生面を考慮して、フィルターを介して行うのが望ましい。フィルターを介した清浄空気は、給気管を介して、処理槽内へ供給される。給気管の中途に設けた給気弁を開閉することで、処理槽内への外気導入の有無が切り替えられる。   The return pressure means is a means for introducing outside air into the treatment tank decompressed by the decompression means and restoring the pressure in the treatment tank. It is desirable to introduce outside air into the treatment tank through a filter in consideration of hygiene. The clean air that has passed through the filter is supplied into the treatment tank via the air supply pipe. By opening and closing an air supply valve provided in the middle of the air supply pipe, the presence or absence of outside air introduction into the processing tank can be switched.

ところで、前記真空弁および/または前記給気弁は、開度調整可能に構成するのが好ましい。この場合、前記減圧手段による処理槽内の減圧、前記復圧手段による処理槽内の復圧について、その各能力が調整可能となる。これにより、減圧手段を一定能力で作動させた状態で、真空弁および/または給気弁の開度を調整して、処理槽内の圧力ひいては温度の調整が容易となる。但し、これに代えてまたはこれに加えて、処理槽内の減圧時に、エゼクタなどの減圧手段自体の減圧能力や作動の有無を制御して、処理槽内の圧力ひいては温度の調整を行うこともできる。   By the way, it is preferable that the vacuum valve and / or the air supply valve are configured to be adjustable in opening. In this case, the respective capacities can be adjusted for the decompression in the treatment tank by the decompression means and the return pressure in the treatment tank by the decompression means. Thereby, in the state which act | operated the pressure reduction means with fixed capability, the opening degree of a vacuum valve and / or an air supply valve is adjusted, and adjustment of the pressure in a processing tank, and temperature is easy. However, instead of this, or in addition to this, when the pressure in the processing tank is reduced, the pressure reducing means such as the ejector itself or the presence or absence of operation can be controlled to adjust the pressure in the processing tank and thus the temperature. it can.

前記排出手段は、処理槽内の蒸気やその凝縮水を外部へ排出する手段である。この排出手段は、処理槽内から蒸気を排出する排蒸管と、スチームトラップを介して処理槽内の底部から凝縮水を排出する排水管とから構成される。ここで、前記排蒸管は、処理槽の底部に接続することで、蒸気に加えてその凝縮水も排出可能となる。処理槽からの排蒸管の中途には、電磁弁などから構成される排蒸弁が設けられる。また、処理槽からの排水管の中途には、電磁弁などから構成される排水弁が設けられる。この排蒸弁および/または排水弁を開閉することで、処理槽内からの蒸気および/または凝縮水の排出の有無が切り替えられる。但し、排蒸弁は開度調整可能に構成してもよく、その場合、排出手段による処理槽外への蒸気排出能力を調整できる。   The discharging means is means for discharging the steam in the processing tank and its condensed water to the outside. This discharge means is comprised from the exhaust steam pipe which discharges | emits a steam from the inside of a processing tank, and the drainage pipe which discharges condensed water from the bottom part in a processing tank via a steam trap. Here, the exhaust pipe is connected to the bottom of the treatment tank, so that the condensed water can be discharged in addition to the steam. In the middle of the exhaust pipe from the treatment tank, an exhaust valve comprising an electromagnetic valve or the like is provided. In addition, a drain valve composed of an electromagnetic valve or the like is provided in the middle of the drain pipe from the treatment tank. By opening and closing the exhaust steam valve and / or drain valve, the presence or absence of the discharge of steam and / or condensed water from the processing tank can be switched. However, the exhaust valve may be configured so that the opening degree can be adjusted, and in that case, the steam discharge capacity to the outside of the processing tank by the discharge means can be adjusted.

上述した給蒸手段、減圧手段、復圧手段、および排出手段などは、制御手段に接続されて制御される。そして、予め設定されたプログラムに従い、所定の運転工程が順次に実行される。この際、処理槽内の圧力を検出する圧力センサからの検出圧力や、経過時間を利用して制御される。また、処理槽内の被加熱物の温度を検出する品温センサを設ける場合には、その品温センサからの検出温度も用いて制御される。   The above-described steam supply means, decompression means, return pressure means, discharge means, and the like are connected to and controlled by the control means. And according to the program set up beforehand, a predetermined operation process is performed one by one. At this time, the control is performed using the detected pressure from the pressure sensor for detecting the pressure in the processing tank and the elapsed time. Moreover, when providing the product temperature sensor which detects the temperature of the to-be-heated material in a processing tank, it controls using the detection temperature from the product temperature sensor.

蒸気加熱装置の運転方法は、特に限定されるものではないが、典型的には空気排除工程の後、加熱工程がなされる。ここで、空気排除工程は、処理槽内に被加熱物を収容した状態で、処理槽内の空気を排出する工程である。具体的には、給蒸弁、給気弁、排蒸弁および排水弁を閉めた状態で、減圧手段を作動させて処理槽内の空気を外部へ吸引排出する。これにより、処理槽内の空気だけでなく、給蒸弁よりも下流側の給蒸管内に溜まっていた空気も排出される。   Although the operating method of a steam heating apparatus is not specifically limited, Typically, a heating process is made after an air exclusion process. Here, an air exclusion process is a process of discharging the air in a processing tank in the state which stored the to-be-heated object in the processing tank. Specifically, with the steam supply valve, the air supply valve, the steam exhaust valve, and the drain valve closed, the pressure reducing means is operated to suck and discharge the air in the processing tank to the outside. Thereby, not only the air in the treatment tank but also the air accumulated in the steam supply pipe on the downstream side of the steam supply valve is discharged.

その後に実行される加熱工程では、給蒸手段により処理槽内へ蒸気を供給して、被加熱物の加熱が図られる。ここで、もしリボイラの起動時など、リボイラ内やそれに続く給蒸管内に空気が溜まっていても、その空気が処理槽内へ供給されないように制御される。すなわち、そのような状態では、上述したように、給蒸弁の直前に設けられた排気弁は開かれている。従って、その溜まっていた空気は、リボイラからの蒸気により排気弁から外部へ押し出され排出される。ところが、リボイラからの蒸気は、前記空気よりも高温であるため、空気排出後は排気弁の開口は閉じられる。そして、その後に給蒸弁を開くことで、処理槽内へ蒸気のみを供給することができる。   In the heating process performed thereafter, steam is supplied into the treatment tank by the steam supply means, and the object to be heated is heated. Here, even when air is accumulated in the reboiler or in the steam supply pipe that follows the reboiler, such as when the reboiler is started up, the air is controlled not to be supplied into the treatment tank. That is, in such a state, as described above, the exhaust valve provided immediately before the steam supply valve is opened. Therefore, the accumulated air is pushed out from the exhaust valve by the steam from the reboiler and discharged. However, since the steam from the reboiler is hotter than the air, the opening of the exhaust valve is closed after the air is discharged. And only a vapor | steam can be supplied in a processing tank by opening a steam supply valve after that.

ところで、リボイラ内の蒸気圧を検出する蒸気圧検出手段の検出信号に基づき、ボイラからリボイラへの蒸気供給を制御することで、リボイラ内の蒸気圧を所望に維持することができる。そして、処理槽内への蒸気供給時には、前記蒸気圧検出手段の検出信号に基づき、リボイラ内の蒸気圧が所望になってから、給蒸弁を開いて処理槽内へ蒸気を供給することができる。リボイラ内の蒸気圧を高めるためには、排気弁を閉じる必要があるが、そのためには上述したように、リボイラや給蒸管内の空気が抜ける必要がある。従って、空気排除したリボイラ内で蒸気圧が高められることになり、リボイラの起動を所望どおり行うことができる。   By the way, the steam pressure in the reboiler can be maintained as desired by controlling the steam supply from the boiler to the reboiler based on the detection signal of the steam pressure detecting means for detecting the steam pressure in the reboiler. Then, when supplying steam into the processing tank, the steam pressure in the reboiler becomes desired based on the detection signal of the steam pressure detecting means, and then the steam supply valve is opened to supply steam into the processing tank. it can. In order to increase the vapor pressure in the reboiler, it is necessary to close the exhaust valve. For this purpose, as described above, the air in the reboiler and the steam supply pipe needs to escape. Therefore, the vapor pressure is increased in the reboiler where air is excluded, and the reboiler can be started as desired.

加熱工程では、処理槽内へ供給する蒸気により、処理槽内の被加熱物の加熱が図られる。この際、処理槽内を大気圧として被加熱物を加熱してもよいし、処理槽内を大気圧より高圧としつつ被加熱物を加熱してもよいし、あるいは所望時に減圧手段を作動させることで大気圧より低圧としつつ被加熱物を加熱してもよい。また、加熱工程においては、処理槽内の圧力もしくは温度、または処理槽内の被加熱物の温度を、目標値に維持するよう制御する。この際、前記目標値は、複数段階に変化させてもよい。   In the heating step, the object to be heated in the processing tank is heated by the steam supplied into the processing tank. At this time, the object to be heated may be heated by setting the inside of the processing tank to atmospheric pressure, the object to be heated may be heated while the inside of the processing tank is set to a pressure higher than atmospheric pressure, or the decompression unit is operated when desired. Thus, the object to be heated may be heated while the pressure is lower than the atmospheric pressure. Moreover, in a heating process, it controls to maintain the pressure or temperature in a processing tank, or the temperature of the to-be-heated material in a processing tank at a target value. At this time, the target value may be changed in a plurality of stages.

そして、加熱工程後には、所望により、真空冷却工程を行ってもよい。この真空冷却工程は、給蒸弁、給気弁、排蒸弁および排水弁を閉じた状態で、減圧手段を作動させて、処理槽内を目標圧力まで減圧して、被加熱物の真空冷却が図られる。   And after a heating process, you may perform a vacuum cooling process if desired. In this vacuum cooling process, with the steam supply valve, the air supply valve, the steam exhaust valve and the drain valve closed, the pressure reducing means is operated to reduce the pressure in the treatment tank to the target pressure, thereby vacuum cooling the object to be heated. Is planned.

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。   Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.

図1は、本発明の蒸気加熱装置の実施例1を示す概略構成図であり、飽和蒸気調理装置に適用した例を示している。この図に示すように、本実施例の飽和蒸気調理装置は、被加熱物としての被調理物(食材または食品)1が収容される中空構造の処理槽2と、この処理槽2内へ蒸気を供給する給蒸手段3と、処理槽2内の気体(空気および/または蒸気)を外部へ吸引排出して処理槽2内を減圧する減圧手段4と、減圧された処理槽2内へ外気を導入して復圧する復圧手段5と、処理槽2内の蒸気やその凝縮水を外部へ排出する排出手段6と、処理槽2内の圧力を計測する圧力センサ7と、この圧力センサ7の出力などに基づき前記各手段3,4,5,6を制御する制御手段8とを備える。   FIG. 1 is a schematic configuration diagram showing a first embodiment of the steam heating apparatus of the present invention, and shows an example applied to a saturated steam cooking apparatus. As shown in this figure, the saturated steam cooking apparatus of the present embodiment includes a processing tank 2 having a hollow structure in which an object to be cooked (food or food) 1 as an object to be heated is accommodated, and steam into the processing tank 2. A steam supply means 3 for supplying gas, a pressure reducing means 4 for sucking and discharging the gas (air and / or steam) in the processing tank 2 to the outside, and reducing the pressure in the processing tank 2, and an outside air into the decompressed processing tank 2 Pressure return means 5 for returning pressure, discharge means 6 for discharging steam and condensed water in the processing tank 2 to the outside, pressure sensor 7 for measuring the pressure in the processing tank 2, and the pressure sensor 7 Control means 8 for controlling the means 3, 4, 5 and 6 based on the output of the above.

本実施例の処理槽2は、一側面へ開口して中空部を有する処理槽本体9と、この処理槽本体9の開口部を開閉する扉10とを備えた金属製の缶体である。このような構成であるから、扉10を閉じることで、処理槽本体9の中空部は密閉される。処理槽2内への被調理物1の収容は、処理槽2に出し入れされるワゴン(不図示)を介して行ってもよいし、図示例のように処理槽2内に棚板11を設けることで対応してもよい。また、被調理物1は、適宜の容器12に入れて、処理槽2内へ収容してもよい。   The processing tank 2 of the present embodiment is a metal can body that includes a processing tank main body 9 that opens to one side surface and has a hollow portion, and a door 10 that opens and closes the opening of the processing tank main body 9. Since it is such a structure, the hollow part of the processing tank main body 9 is sealed by closing the door 10. FIG. The to-be-cooked object 1 may be accommodated in the processing tank 2 via a wagon (not shown) that is taken in and out of the processing tank 2, or a shelf plate 11 is provided in the processing tank 2 as shown in the illustrated example. You may respond by doing. Moreover, the to-be-cooked object 1 may be accommodated in the processing tank 2 in an appropriate container 12.

処理槽2内の圧力を検出するために、処理槽2には圧力センサ7が設けられる。但し、圧力センサ7に代えて、温度センサ(不図示)を用いてもよい。圧力と温度とを換算することで、いずれのセンサでも利用可能である。また、処理槽2内に収容される被調理物1の温度を検出するために、品温センサ(不図示)をさらに設けてもよい。   In order to detect the pressure in the processing tank 2, a pressure sensor 7 is provided in the processing tank 2. However, a temperature sensor (not shown) may be used instead of the pressure sensor 7. Any sensor can be used by converting pressure and temperature. Moreover, in order to detect the temperature of the to-be-cooked object 1 accommodated in the processing tank 2, you may further provide a product temperature sensor (not shown).

処理槽2内へ蒸気を供給するために、処理槽2には給蒸手段3が接続される。本実施例の給蒸手段3は、ボイラ(一次ボイラ)13とリボイラ(二次ボイラ)14とを備え、ボイラ13からの蒸気を熱源として、リボイラ14にて軟水を蒸気化し、そのようにして生成された清浄蒸気が処理槽2内へ供給される。通常、ボイラ13による蒸気には、配管内の錆や、防錆剤などのボイラ水処理薬品が混入するおそれが残る。ところが、処理槽2内へ供給される蒸気は、直接に被調理物1に接触し得るものである。そこで、リボイラ14にて軟水を蒸気化し、その清浄蒸気を処理槽2内へ供給する。   In order to supply steam into the treatment tank 2, steam supply means 3 is connected to the treatment tank 2. The steam supply means 3 of the present embodiment includes a boiler (primary boiler) 13 and a reboiler (secondary boiler) 14, vaporizes soft water in the reboiler 14 using the steam from the boiler 13 as a heat source, and so on. The generated clean steam is supplied into the treatment tank 2. Normally, there is a risk that the steam generated by the boiler 13 is mixed with rust in the pipe or boiler water treatment chemicals such as a rust inhibitor. However, the steam supplied into the treatment tank 2 can directly come into contact with the object 1 to be cooked. Therefore, the reboiler 14 vaporizes the soft water and supplies the clean steam into the treatment tank 2.

リボイラ14は、ステンレス製の熱交換器であり、その缶体15内に供給された軟水を、ボイラ13からの蒸気で加熱して蒸気化する。ボイラ13からの蒸気は、缶体15内に配置された蒸気供給管16内を通され、周囲に貯留された軟水を加熱する。この蒸気供給管16内への蒸気供給の有無は、電磁弁から構成されるリボイラ弁17を開閉することで制御される。また、蒸気供給管16内へ供給された蒸気の凝縮水は、スチームトラップ18を介して排出される。ところで、リボイラ14の缶体15内へは、給水ポンプ19を介して軟水が供給可能とされ、その給水ポンプ19を制御することで、缶体15内の水位は自動調整される。   The reboiler 14 is a stainless steel heat exchanger, and the soft water supplied into the can 15 is heated with the steam from the boiler 13 to be vaporized. The steam from the boiler 13 is passed through the steam supply pipe 16 disposed in the can 15 to heat the soft water stored in the surroundings. Whether or not the steam is supplied into the steam supply pipe 16 is controlled by opening and closing a reboiler valve 17 constituted by an electromagnetic valve. Further, the condensed water of the steam supplied into the steam supply pipe 16 is discharged through the steam trap 18. By the way, soft water can be supplied into the can body 15 of the reboiler 14 via the water supply pump 19, and the water level in the can body 15 is automatically adjusted by controlling the water supply pump 19.

さらに、リボイラ14には、制御圧力スイッチ20と低圧圧力スイッチ21とが設けられる。制御圧力スイッチ20は、缶体15内の蒸気圧を所望に維持するために、その上限値と下限値とを検知する。この制御圧力スイッチ20の検出信号に基づき、前記リボイラ弁17を開閉制御することで、リボイラ14内は所望の蒸気圧に維持される。また、低圧圧力スイッチ21は、缶体15内の圧力が何らかの理由で所定値を下回った場合に、それに基づき異常を検知する。   Further, the reboiler 14 is provided with a control pressure switch 20 and a low pressure switch 21. The control pressure switch 20 detects the upper limit value and the lower limit value in order to maintain the vapor pressure in the can 15 as desired. The reboiler 14 is maintained at a desired vapor pressure by controlling the opening and closing of the reboiler valve 17 based on the detection signal of the control pressure switch 20. Further, the low pressure switch 21 detects an abnormality based on the pressure in the can 15 that falls below a predetermined value for some reason.

リボイラ14からの清浄蒸気は、給蒸管22を介して処理槽2内へ供給される。本実施例では、給蒸管22から処理槽2内への蒸気供給は、給蒸管22の末端部に設けたノズル23から蒸気を噴出させて行うが、このノズル23は省略可能である。   Clean steam from the reboiler 14 is supplied into the processing tank 2 through the steam supply pipe 22. In this embodiment, the steam supply from the steam supply pipe 22 into the processing tank 2 is performed by jetting steam from a nozzle 23 provided at the end of the steam supply pipe 22, but this nozzle 23 can be omitted.

給蒸管22の中途には、給蒸弁24が開閉可能に設けられる。この給蒸弁24は、モータバルブや比例制御弁のように、開度調整可能な構成が好ましい。但し、処理槽2内への蒸気供給の有無を切り替え可能な構成であれば足り、開度調整が不能で開放または閉鎖のいずれかの状態を採る電磁弁により構成してもよい。いずれにしても、この給蒸弁24を開閉操作することで、処理槽2内の圧力ひいては温度を調整することができる。また、処理槽2内の圧力調整は、給蒸弁24だけでなく減圧手段4を制御することによっても行うことができる。   A steam supply valve 24 is provided in the middle of the steam supply pipe 22 so as to be openable and closable. The steam supply valve 24 is preferably configured such that the opening can be adjusted, such as a motor valve or a proportional control valve. However, any configuration that can switch the presence / absence of supply of steam into the processing tank 2 is sufficient, and the opening degree cannot be adjusted, and an electromagnetic valve that takes either an open state or a closed state may be used. In any case, by opening and closing the steam supply valve 24, the pressure in the processing tank 2 and thus the temperature can be adjusted. Moreover, the pressure in the processing tank 2 can be adjusted by controlling not only the steam supply valve 24 but also the decompression means 4.

さらに、給蒸管22には、給蒸弁24よりも上流側(リボイラ14側)で且つ給蒸弁24に近接して、排気弁25が設けられる。この排気弁25は、給蒸管22の外周壁を介して給蒸管22の内外を連通するよう開口するが、リボイラ14から蒸気が供給されると、その温度を検知して開口を閉じる構成である。   Further, the steam supply pipe 22 is provided with an exhaust valve 25 on the upstream side (reboiler 14 side) of the steam supply valve 24 and in the vicinity of the steam supply valve 24. The exhaust valve 25 opens so as to communicate the inside and outside of the steam supply pipe 22 through the outer peripheral wall of the steam supply pipe 22. When steam is supplied from the reboiler 14, the temperature is detected and the opening is closed. It is.

本実施例の排気弁25は、温調トラップから構成される。使用される温調トラップ25は、特に問わないが、本実施例では、たとえば株式会社ミヤワキ製のダイヤフラム式スチームトラップ、Dシリーズ「DC1−21H」などが使用される。この温調トラップ25は、設置箇所の圧力下における飽和蒸気温度より所定温度(たとえば5℃)低い温度で作動して、開口を閉じる構成である。   The exhaust valve 25 of this embodiment is composed of a temperature control trap. The temperature control trap 25 used is not particularly limited. In this embodiment, for example, a diaphragm type steam trap manufactured by Miyawaki Co., Ltd., D series “DC1-21H” or the like is used. The temperature control trap 25 is configured to operate at a temperature lower by a predetermined temperature (for example, 5 ° C.) than the saturated steam temperature under the pressure at the installation location and close the opening.

従って、リボイラ14の起動時など、給蒸管22内が空気で満たされていると、排気弁25は開口して大気圧下にある。そのため、その飽和蒸気温度の100℃から前記所定温度だけ低い温度(たとえば95℃)まで、リボイラ14からの蒸気で温められると、温調トラップ25が作動してその開口が閉じられる。   Therefore, when the inside of the steam supply pipe 22 is filled with air, such as when the reboiler 14 is activated, the exhaust valve 25 opens and is under atmospheric pressure. Therefore, when warmed by the steam from the reboiler 14 from 100 ° C. of the saturated steam temperature to a temperature lower by the predetermined temperature (for example, 95 ° C.), the temperature control trap 25 is activated and the opening is closed.

温調トラップからなる排気弁25は、給蒸管22の水平配管部の上周面などに、直付けして設置される。これにより、給蒸管22内に蒸気が流れている際に、その蒸気の温度を低下させることなく検知でき、しかもドレンの排出を防止して空気のみを排出させることができる。   The exhaust valve 25 composed of a temperature control trap is directly attached to the upper peripheral surface of the horizontal piping portion of the steam supply pipe 22 or the like. As a result, when steam flows in the steam supply pipe 22, it can be detected without lowering the temperature of the steam, and drainage can be prevented and only air can be discharged.

処理槽2には、処理槽2内の空気や蒸気を外部へ吸引排出して、処理槽2内を減圧する減圧手段4が接続される。本実施例では、処理槽2からの排気管26には、処理槽2の側から順に、真空弁27、蒸気エゼクタ28、熱交換器29、逆止弁30、および水封式真空ポンプ31が接続される。真空弁27は、電磁弁でもよいが、比例制御弁やモータバルブのように開度調整可能な構成が好ましい。   The processing tank 2 is connected to a decompression unit 4 that sucks and discharges air and vapor in the processing tank 2 to the outside and decompresses the processing tank 2. In this embodiment, a vacuum valve 27, a steam ejector 28, a heat exchanger 29, a check valve 30, and a water-sealed vacuum pump 31 are provided in the exhaust pipe 26 from the processing tank 2 in this order from the processing tank 2 side. Connected. The vacuum valve 27 may be an electromagnetic valve, but preferably has a configuration in which the opening degree can be adjusted, such as a proportional control valve or a motor valve.

真空ポンプ31には、封水給水弁32を介して水が供給され、真空ポンプ31からの排水は、排水口(不図示)へ排出される。この封水給水弁32は、真空ポンプ31に連動して開かれる。また、熱交換器29にも、熱交給水弁33を介して水が供給され、排水口へ排水される。熱交換器29に冷却用水が供給されることで、排気管26内の蒸気を冷却し凝縮させることができる。   Water is supplied to the vacuum pump 31 via a sealed water supply valve 32, and the waste water from the vacuum pump 31 is discharged to a drain port (not shown). The sealed water supply valve 32 is opened in conjunction with the vacuum pump 31. Further, water is also supplied to the heat exchanger 29 via the heat exchange water supply valve 33 and drained to the drain outlet. By supplying the cooling water to the heat exchanger 29, the steam in the exhaust pipe 26 can be cooled and condensed.

処理槽2には、減圧手段4にて減圧された後、復圧するための復圧手段5が接続される。本実施例の復圧手段5は、処理槽2に接続された給気管34が、逆止弁35および除菌フィルター36を介して外気と連通可能に設けられている。この給気管34の中途には、給気弁37が開閉可能に設けられており、この給気弁37の開放により、処理槽2内は大気圧に開放可能とされる。   The treatment tank 2 is connected to a decompression means 5 for decompressing after the decompression by the decompression means 4. In the return pressure means 5 of the present embodiment, an air supply pipe 34 connected to the processing tank 2 is provided so as to be able to communicate with outside air via a check valve 35 and a sterilization filter 36. A supply valve 37 is provided in the middle of the supply pipe 34 so as to be openable and closable. By opening the supply valve 37, the inside of the processing tank 2 can be opened to atmospheric pressure.

処理槽2には、処理槽2内の蒸気やその凝縮水を外部へ排出するための排出手段6が接続される。この排出手段6は、処理槽2内の蒸気や空気を外部へ排出するための排蒸手段38と、処理槽2内に生じた凝縮水を外部へ排出するための排水手段39とに分けられる。   The treatment tank 2 is connected to a discharge means 6 for discharging the steam in the treatment tank 2 and its condensed water to the outside. The discharging means 6 is divided into a steaming means 38 for discharging steam and air in the processing tank 2 to the outside, and a draining means 39 for discharging condensed water generated in the processing tank 2 to the outside. .

排蒸手段38は、排蒸管40を介して処理槽2内の空気や蒸気を処理槽2外へ導出する手段である。排蒸管40の中途には排蒸弁41が設けられ、この排蒸弁41も開度調整可能な構成が好ましい。図示例では、処理槽2の下部に排蒸管40を接続しているが、これに代えてまたはこれに加えて、処理槽2の上部にも同様の排蒸管(不図示)を設けることができる。処理槽2の下部からの排蒸管40は、処理槽2内の下部に溜まる凝縮水を外部へ排出するためにも利用できる。   The steaming means 38 is a means for leading the air and steam in the processing tank 2 to the outside of the processing tank 2 through the steaming pipe 40. An exhaust steam valve 41 is provided in the middle of the exhaust pipe 40, and the exhaust valve 41 is preferably configured so that its opening degree can be adjusted. In the illustrated example, the exhaust pipe 40 is connected to the lower part of the processing tank 2, but a similar exhaust pipe (not shown) is provided at the upper part of the processing tank 2 instead of or in addition to this. Can do. The exhaust pipe 40 from the lower part of the processing tank 2 can also be used for discharging condensed water accumulated in the lower part of the processing tank 2 to the outside.

一方、排水手段39は、スチームトラップ42を有する排水管43からなり、この排水管43を介して処理槽2内の底部に溜まる凝縮水は、処理槽2外へ排水可能とされる。そして、この排水管43の中途には、電磁弁から構成される排水弁44が設けられる。   On the other hand, the drainage means 39 includes a drain pipe 43 having a steam trap 42, and the condensed water accumulated at the bottom of the processing tank 2 can be drained out of the processing tank 2 through the drain pipe 43. And in the middle of this drain pipe 43, the drain valve 44 comprised from an electromagnetic valve is provided.

前記給蒸手段3、前記減圧手段4、前記復圧手段5、前記排出手段6などは、制御手段8により制御される。この制御手段8は、それが把握する経過時間や前記圧力センサ7および各圧力スイッチ20,21からの検出信号などに基づいて、前記各手段3,4,5,6を制御する制御器45である。具体的には、リボイラ弁17、給水ポンプ19、給蒸弁24、真空弁27、真空ポンプ31、封水給水弁32、熱交給水弁33、給気弁37、排蒸弁41、排水弁44、圧力センサ7および各圧力スイッチ20,21などは、制御器45に接続される。   The steam supply means 3, the decompression means 4, the return pressure means 5, the discharge means 6 and the like are controlled by a control means 8. This control means 8 is a controller 45 that controls each of the means 3, 4, 5, 6 based on the elapsed time grasped by it, detection signals from the pressure sensor 7 and the pressure switches 20, 21 and the like. is there. Specifically, the reboiler valve 17, the feed water pump 19, the steam feed valve 24, the vacuum valve 27, the vacuum pump 31, the sealed water feed water valve 32, the heat exchange water feed valve 33, the air feed valve 37, the steam feed valve 41, and the drain valve 44, the pressure sensor 7, the pressure switches 20 and 21, and the like are connected to the controller 45.

そして、制御器45は、所定の手順(プログラム)に従い、処理槽2内の被調理物1の加熱調理を行う。加熱調理しようとする場合、まず被調理物1を処理槽2内に収容し、処理槽2の扉10を閉じる。この初期状態では、給蒸弁24、真空弁27、封水給水弁32、熱交給水弁33は閉じられ、蒸気エゼクタ28および真空ポンプ31は作動を停止しており、給気弁37、排蒸弁41および排水弁44は開かれている。そして、この状態から、典型的には、処理槽2内の空気を排除する空気排除工程、処理槽2内へ蒸気を供給して被調理物1の加熱調理を図る加熱工程、および処理槽2内を大気圧まで復圧する復圧工程、が順次に実行される。   And the controller 45 performs the heating cooking of the to-be-cooked object 1 in the processing tank 2 according to a predetermined procedure (program). When cooking by heating, first, the cooking object 1 is accommodated in the processing tank 2 and the door 10 of the processing tank 2 is closed. In this initial state, the steam supply valve 24, the vacuum valve 27, the sealed water supply valve 32, and the heat exchange water supply valve 33 are closed, and the operation of the steam ejector 28 and the vacuum pump 31 is stopped. The steam valve 41 and the drain valve 44 are open. And typically from this state, the air removal process which excludes the air in the processing tank 2, the heating process which supplies the vapor | steam to the processing tank 2, and heat-cookes the to-be-cooked object 1, and the processing tank 2 A return pressure process for returning the pressure to the atmospheric pressure is sequentially performed.

空気排除工程では、制御器45は、給蒸弁24、給気弁37、排蒸弁41および排水弁44を閉じた状態で、減圧手段4を作動させる。すなわち、封水給水弁32を開いて真空ポンプ31を作動させると共に、真空弁27を開いて処理槽2内の空気を外部へ吸引排出する。ここで、処理槽2内を所定圧力まで減圧した後、蒸気エゼクタ28を作動させてもよい。また、熱交給水弁33を開くことで、熱交換器29にて蒸気を凝縮させて、減圧能力を高めることができる。   In the air exclusion process, the controller 45 operates the pressure reducing means 4 with the steam supply valve 24, the air supply valve 37, the exhaust steam valve 41 and the drain valve 44 closed. That is, the sealed water supply valve 32 is opened to operate the vacuum pump 31, and the vacuum valve 27 is opened to suck and discharge the air in the processing tank 2 to the outside. Here, the steam ejector 28 may be operated after the inside of the treatment tank 2 is depressurized to a predetermined pressure. In addition, by opening the heat exchange water supply valve 33, the heat exchanger 29 can condense the steam and increase the decompression capacity.

このような処理槽2内からの空気排除は、圧力センサ7を利用することで、設定圧力まで行ってもよいし、あるいは設定時間だけ行うようにしてもよい。そして、制御器45は、蒸気エゼクタ28および真空ポンプ31の作動を停止させると共に、封水給水弁32、熱交給水弁33、および真空弁27を閉じて、空気排除工程を終了する。   Such air exclusion from the processing tank 2 may be performed up to a set pressure by using the pressure sensor 7 or may be performed only for a set time. Then, the controller 45 stops the operation of the steam ejector 28 and the vacuum pump 31, closes the sealed water supply valve 32, the heat exchange water supply valve 33, and the vacuum valve 27, and ends the air exclusion process.

次工程の加熱工程では、制御器45は、給蒸弁24を開いて処理槽2内へ蒸気を供給する。但し、リボイラ14への初期給水時や、ボイラ13からリボイラ14への初期給蒸時など、リボイラ14や給蒸管22内に空気が溜まっている場合には、まずその空気が排気弁25から外部へ排出された後、処理槽2内へ蒸気が供給される。   In the next heating process, the controller 45 opens the steam supply valve 24 to supply steam into the processing tank 2. However, when air is accumulated in the reboiler 14 or the steam supply pipe 22 at the time of initial water supply to the reboiler 14 or at the time of initial steaming from the boiler 13 to the reboiler 14, first, the air is discharged from the exhaust valve 25 After being discharged to the outside, steam is supplied into the processing tank 2.

すなわち、リボイラ14の起動時など、給蒸管22内に空気が溜まっている状態では、まだ温度が上がっていないために、排気弁25は開いた状態とされている。従って、給蒸管22内などに溜まっていた空気は、リボイラ14からの蒸気により排気弁25から外部へ押し出され排出される。そして、空気が抜ければ温度が上がるため、その後の運転中は排気弁25が閉まった状態に維持される。制御器45は、排気弁25から空気排除した後、給蒸弁24を開くことで、処理槽2内への空気の流入を防止する。具体的には、次に述べるように、排気弁25が閉じられた後、リボイラ14内の蒸気圧が所望まで高められたことを確認後、給蒸弁24を開いて処理槽2内へ蒸気供給する。   That is, when the reboiler 14 is activated or the like, in a state where air is accumulated in the steam supply pipe 22, the temperature has not yet risen, so the exhaust valve 25 is open. Therefore, the air accumulated in the steam supply pipe 22 is pushed out from the exhaust valve 25 by the steam from the reboiler 14 and discharged. Since the temperature rises when air is released, the exhaust valve 25 is kept closed during the subsequent operation. The controller 45 prevents the inflow of air into the processing tank 2 by opening the steam supply valve 24 after removing air from the exhaust valve 25. Specifically, as described below, after confirming that the vapor pressure in the reboiler 14 has been increased to a desired level after the exhaust valve 25 is closed, the steam supply valve 24 is opened and steam enters the treatment tank 2. Supply.

上述したように、リボイラ14および給蒸管22内の空気が排気弁25から排出後、リボイラ14からの蒸気の温度に基づき、排気弁25が閉じられる。その状態で、制御器45は、蒸気圧検出手段としての制御圧力スイッチ20の検出信号を利用して、リボイラ弁17の開閉を制御することで、リボイラ14内の蒸気圧を所望に高めて維持する。リボイラ14内の蒸気圧が所望にまで高められると、制御器45は、制御圧力スイッチ20からの検出信号に基づき給蒸弁24の開放を可能とし、処理槽2内の被調理物1の加熱調理を開始する。   As described above, after the air in the reboiler 14 and the steam supply pipe 22 is discharged from the exhaust valve 25, the exhaust valve 25 is closed based on the temperature of the steam from the reboiler 14. In this state, the controller 45 controls the opening and closing of the reboiler valve 17 using the detection signal of the control pressure switch 20 as the vapor pressure detecting means, thereby increasing and maintaining the vapor pressure in the reboiler 14 as desired. To do. When the vapor pressure in the reboiler 14 is increased to a desired level, the controller 45 enables the steam supply valve 24 to be opened based on the detection signal from the control pressure switch 20 and heats the cooking object 1 in the treatment tank 2. Start cooking.

加熱工程では、真空弁27、封水給水弁32、熱交給水弁33、給気弁37、排蒸弁41を閉じると共に、蒸気エゼクタ28および真空ポンプ31の作動を停止した状態で、給蒸弁24を開いて処理槽2内へ蒸気供給する。この際、処理槽2内が大気圧を超える場合、排水弁44を開くことで、処理槽2内の底部から凝縮水を外部へ排出する。   In the heating process, the vacuum valve 27, the sealed water supply valve 32, the heat exchange water supply valve 33, the air supply valve 37, and the exhaust valve 41 are closed, and the steam ejector 28 and the vacuum pump 31 are stopped from operating. The valve 24 is opened to supply steam into the treatment tank 2. At this time, when the inside of the treatment tank 2 exceeds the atmospheric pressure, the drain valve 44 is opened to discharge condensed water from the bottom of the treatment tank 2 to the outside.

このようにして、処理槽2内が所望の設定圧力になるまで、給蒸手段3により処理槽2内へ蒸気供給する。そして、処理槽2内を設定圧力に保持するように、圧力センサ7の検出圧力に基づき給蒸手段3による処理槽2内への蒸気供給を調整して、処理槽2内の被調理物1の加熱調理が図られる。この加熱工程中、設定圧力を段階的に上下に変化させてもよい。   In this way, steam is supplied into the processing tank 2 by the steam supply means 3 until the inside of the processing tank 2 reaches a desired set pressure. And the steam supply to the processing tank 2 by the steam supply means 3 is adjusted based on the detected pressure of the pressure sensor 7 so that the inside of the processing tank 2 is kept at the set pressure, and the cooked object 1 in the processing tank 2 Is cooked. During this heating process, the set pressure may be changed up and down stepwise.

ところで、処理槽2内へ蒸気供給して行う被調理物1の加熱調理は、大気圧下で行う無圧蒸煮と、大気圧を超える圧力で行う加圧蒸煮と、所望時に減圧手段4を作動させて大気圧未満の圧力で行う減圧蒸煮とがある。   By the way, the cooking of the object 1 to be cooked by supplying steam into the treatment tank 2 is performed by pressureless cooking performed at atmospheric pressure, pressure cooking performed at a pressure exceeding atmospheric pressure, and the decompression means 4 operated when desired. And steaming under reduced pressure at a pressure lower than atmospheric pressure.

無圧蒸煮の場合、真空弁27、封水給水弁32、熱交給水弁33、給気弁37を閉じると共に、蒸気エゼクタ28および真空ポンプ31の作動を停止した状態で、給蒸弁24、排蒸弁41、排水弁44を開いて、処理槽2内へ蒸気を供給し排出する。   In the case of non-pressure steaming, the vacuum valve 27, the sealed water supply valve 32, the heat exchange water supply valve 33, the air supply valve 37 are closed, and the steam ejector 28 and the vacuum pump 31 are stopped, and the steam supply valve 24, The steam exhaust valve 41 and the drain valve 44 are opened to supply and discharge steam into the treatment tank 2.

加圧蒸煮の場合、真空弁27、封水給水弁32、熱交給水弁33、給気弁37、排蒸弁41を閉じると共に、蒸気エゼクタ28および真空ポンプ31の作動を停止した状態で、給蒸弁24、排水弁44を開いて、処理槽2内へ蒸気を供給する。従って、加圧蒸煮の場合には、排水管43から自動的に凝縮水が外部へ排出される。   In the case of pressurized steaming, the vacuum valve 27, the sealed water supply valve 32, the heat exchange water supply valve 33, the air supply valve 37, and the exhaust steam valve 41 are closed, and the operation of the steam ejector 28 and the vacuum pump 31 is stopped. The steam supply valve 24 and the drain valve 44 are opened to supply steam into the treatment tank 2. Therefore, in the case of pressurized steaming, the condensed water is automatically discharged from the drain pipe 43 to the outside.

減圧蒸煮の場合は、給気弁37、排蒸弁41、排水弁44を閉じた状態で、給蒸弁24を開いて、処理槽2内へ蒸気を供給する。この際、処理槽2内が設定上限圧力を超えると、減圧手段4を作動させて、設定下限圧力まで処理槽2内を減圧する。すなわち、真空弁27、封水給水弁32、熱交給水弁33を開いた状態で、真空ポンプ31(場合によりさらに蒸気エゼクタ28)を作動させて、設定下限圧力まで処理槽2内を減圧し、設定下限圧力になると、これら各弁27,32,33を閉じると共に真空ポンプ31などの作動を停止する。   In the case of steaming under reduced pressure, the steam supply valve 24 is opened and the steam is supplied into the processing tank 2 with the air supply valve 37, the exhaust steam valve 41 and the drain valve 44 being closed. At this time, when the inside of the treatment tank 2 exceeds the set upper limit pressure, the decompression means 4 is operated to decompress the inside of the treatment tank 2 to the set lower limit pressure. That is, with the vacuum valve 27, the sealed water supply valve 32, and the heat exchange water supply valve 33 opened, the vacuum pump 31 (or the steam ejector 28 in some cases) is operated to reduce the inside of the treatment tank 2 to the set lower limit pressure. When the set lower limit pressure is reached, the valves 27, 32 and 33 are closed and the operation of the vacuum pump 31 and the like is stopped.

いずれの場合も、基本的には、蒸気供給による処理槽2内の加圧要因と、供給された蒸気の凝縮による処理槽2内の減圧要因とがバランスを保つように、給蒸弁24の開閉を制御して、処理槽2内の圧力を目標値に維持して加熱調理がなされる。但し、減圧蒸煮の場合には、設定上限圧力を超えると、上述のとおり減圧手段4を作動させる場合がある。   In any case, basically, in order to keep a balance between the pressurizing factor in the processing tank 2 due to the supply of steam and the depressurizing factor in the processing tank 2 due to the condensation of the supplied steam, The cooking is performed by controlling the opening and closing to maintain the pressure in the treatment tank 2 at the target value. However, in the case of reduced-pressure steaming, if the set upper limit pressure is exceeded, the decompression means 4 may be operated as described above.

このようにして、加熱工程では、処理槽2内へ蒸気が供給されることで、処理槽2内に収容された被調理物1を加熱調理することができる。この際、上述したように、処理槽2内へ供給される蒸気は、リボイラ14にて軟水から生成された清浄蒸気である。従って、安全で安心の加熱調理を実現することができる。また、被調理物1の全周囲に清浄蒸気を行き渡らせることで、短時間で均一の加熱料理がなされる。   In this way, in the heating process, the cooking object 1 accommodated in the processing tank 2 can be cooked by supplying steam into the processing tank 2. At this time, as described above, the steam supplied into the treatment tank 2 is clean steam generated from soft water in the reboiler 14. Therefore, safe and reliable cooking can be realized. Moreover, uniform heating cooking is made in a short time by spreading clean steam around the entire periphery of the object 1 to be cooked.

加熱工程では、処理槽2内への蒸気供給により処理槽2内の圧力を調整することで、処理槽2内の温度を調整することができる。本実施例では、たとえば60℃から130℃の範囲にて、自由な温度に設定して加熱調理を可能としている。このようにして処理槽2の圧力を調整することで、飽和蒸気温度が調整される。   In the heating step, the temperature in the processing tank 2 can be adjusted by adjusting the pressure in the processing tank 2 by supplying steam into the processing tank 2. In the present embodiment, cooking is possible by setting the temperature freely, for example, in the range of 60 ° C to 130 ° C. In this way, the saturated steam temperature is adjusted by adjusting the pressure of the treatment tank 2.

そして、加熱工程の終了後の復圧工程では、給蒸弁24が閉じられる。そして、処理槽2内が大気圧を超える圧力であれば、排蒸弁41を開いて、処理槽2内が大気圧になるまで、排水および排蒸がなされる。一方、処理槽2内が大気圧未満であれば、減圧手段4および排出手段6を作動させず、かつ、給蒸弁24を閉じると共に給気弁37を開いて、処理槽2内を大気圧まで復圧する。その後、処理槽2の扉10を開いて、処理槽2内から被調理物1を取り出して、一連の処理を完了する。   And in the pressure-recovery process after completion | finish of a heating process, the steam supply valve 24 is closed. And if the inside of the processing tank 2 exceeds the atmospheric pressure, the exhaust steam valve 41 is opened, and drainage and exhaust are performed until the inside of the processing tank 2 reaches the atmospheric pressure. On the other hand, if the inside of the processing tank 2 is less than the atmospheric pressure, the decompression means 4 and the discharge means 6 are not operated, the steam supply valve 24 is closed and the air supply valve 37 is opened to Restore pressure until Then, the door 10 of the processing tank 2 is opened, the to-be-cooked object 1 is taken out from the processing tank 2, and a series of processes is completed.

本発明の蒸気加熱装置は、前記実施例の構成に限らず、適宜変更可能である。たとえば、前記実施例では、飽和蒸気調理装置に適用した例を示したが、手術用メスなどを蒸気加熱により滅菌するための蒸気滅菌装置などにも、同様に適用可能である。あるいは、前記加熱工程後に、処理槽2内を減圧手段4により減圧して、被調理物1の真空冷却を図る蒸煮冷却機とすることもできる。   The steam heating apparatus of the present invention is not limited to the configuration of the above embodiment, and can be changed as appropriate. For example, although the example applied to the saturated steam cooking apparatus has been described in the above embodiment, the present invention can be similarly applied to a steam sterilization apparatus for sterilizing a scalpel for operation by steam heating. Or after the said heating process, it can also be set as the steaming cooler which decompresses the inside of the processing tank 2 with the decompression means 4, and performs the vacuum cooling of the to-be-cooked object 1. FIG.

また、前記実施例では、ボイラ13からの蒸気を用いてリボイラ14にて軟水を蒸気化する構成としたが、リボイラ14を用いずにボイラ13からの蒸気を直接に処理槽2内へ供給する際にも、同様に適用可能である。さらに、前記実施例では、減圧手段4として、蒸気エゼクタ28と熱交換器29と水封式真空ポンプ31とを用いたが、これらは一例であり適宜変更可能である。たとえば、蒸気エゼクタ28は省略してもよい。   Moreover, in the said Example, although it was set as the structure which vaporizes soft water with the reboiler 14 using the steam from the boiler 13, the steam from the boiler 13 is directly supplied in the process tank 2 without using the reboiler 14. The same applies to the case. Furthermore, in the said Example, although the steam ejector 28, the heat exchanger 29, and the water seal vacuum pump 31 were used as the pressure reduction means 4, these are examples and can be changed suitably. For example, the steam ejector 28 may be omitted.

さらに、前記実施例では、排気弁として温調トラップ25を用いたが、温調トラップ25に代えて、温度センサ46と開閉弁47の組合せを用いてもよい。この場合、図2に示すように、給蒸管22の中途部には、給蒸弁24と近接した位置に、短い分岐管48を接続し、この分岐管48に排気弁として電磁弁などからなる開閉弁47を配置する。従って、開閉弁47を開いた状態では、給蒸管22の内外が連通される。そして、この開閉弁47は、給蒸弁24より上流側の給蒸管22内に設けた温度センサ46の検出信号に基づき、開閉制御される。すなわち、設定温度未満の場合には、前記開閉弁47を開口する一方、設定温度以上の場合には前記開閉弁47を閉鎖する。ところで、図2では、給蒸管22の中途部のみを示したが、その他の構成は図1と同様である。この構成の場合も、開閉弁47からなる排気弁47により、リボイラ14や給蒸管22内の空気を排除した後、処理槽2内へ蒸気のみを供給可能となる。   Furthermore, in the above-described embodiment, the temperature control trap 25 is used as the exhaust valve. However, a combination of the temperature sensor 46 and the on-off valve 47 may be used instead of the temperature control trap 25. In this case, as shown in FIG. 2, a short branch pipe 48 is connected to the middle of the steam supply pipe 22 at a position close to the steam supply valve 24, and an electromagnetic valve or the like is connected to the branch pipe 48 as an exhaust valve. An on-off valve 47 is arranged. Therefore, when the on-off valve 47 is opened, the inside and outside of the steam supply pipe 22 are communicated. The opening / closing valve 47 is controlled to open / close based on a detection signal from a temperature sensor 46 provided in the steam supply pipe 22 upstream of the steam supply valve 24. That is, when the temperature is lower than the set temperature, the on-off valve 47 is opened, and when the temperature is higher than the set temperature, the on-off valve 47 is closed. By the way, in FIG. 2, only the middle part of the steam supply pipe 22 is shown, but other configurations are the same as those in FIG. Also in this configuration, only the steam can be supplied into the treatment tank 2 after the air in the reboiler 14 and the steam supply pipe 22 is removed by the exhaust valve 47 including the on-off valve 47.

本発明の蒸気加熱装置の一実施例を示す概略構成図である。It is a schematic block diagram which shows one Example of the steam heating apparatus of this invention. 図1の蒸気加熱装置における排気弁の変形例を示す図であり、給蒸管の部分のみを示している。It is a figure which shows the modification of the exhaust valve in the steam heating apparatus of FIG. 1, and has shown only the part of the steam supply pipe | tube.

符号の説明Explanation of symbols

1 被調理物(被加熱物)
2 処理槽
4 減圧手段
8 制御手段
13 ボイラ
14 リボイラ(蒸気発生装置)
20 制御圧力スイッチ(蒸気圧検出手段)
22 給蒸管
24 給蒸弁
25 温調トラップ(排気弁)
46 温度センサ(管内温度検出手段)
47 開閉弁(排気弁)
1 To-be-cooked object (object to be heated)
2 Processing tank 4 Pressure reducing means 8 Control means 13 Boiler 14 Reboiler (steam generator)
20 Control pressure switch (Vapor pressure detection means)
22 Steam supply pipe 24 Steam supply valve 25 Temperature control trap (exhaust valve)
46 Temperature sensor (In-pipe temperature detection means)
47 On-off valve (exhaust valve)

Claims (5)

被加熱物が収容される処理槽と、
この処理槽内へ蒸気発生装置からの蒸気を供給する給蒸管と、
この給蒸管に設けられ、その管路を開閉する給蒸弁と、
この給蒸弁より前記蒸気発生装置側の前記給蒸管に設けられ、設定温度未満では前記給蒸管の内外を連通するよう開口する一方、設定温度以上では前記開口を閉鎖する排気弁と
を備えることを特徴とする蒸気加熱装置。
A treatment tank in which an object to be heated is accommodated;
A steam supply pipe for supplying steam from the steam generator into the treatment tank;
A steam supply valve that is provided in the steam supply pipe and opens and closes the pipeline;
An exhaust valve that is provided in the steam supply pipe on the steam generator side from the steam supply valve and opens to communicate with the inside and outside of the steam supply pipe at a temperature lower than a set temperature, and closes the opening at a temperature higher than the set temperature. A steam heating apparatus comprising:
前記処理槽内の空気を外部へ吸引排出する減圧手段と、
前記蒸気発生装置内の蒸気圧を検出する蒸気圧検出手段と、
この蒸気圧検出手段の検出信号に基づき前記給蒸弁の開閉を制御する制御手段と
をさらに備えることを特徴とする請求項1に記載の蒸気加熱装置。
Decompression means for sucking and discharging the air in the treatment tank to the outside;
A vapor pressure detecting means for detecting a vapor pressure in the steam generator;
The steam heating apparatus according to claim 1, further comprising: a control unit that controls opening and closing of the steam supply valve based on a detection signal of the steam pressure detection unit.
被加熱物が収容される処理槽と、
ボイラからの蒸気を熱源として軟水または純水を蒸気とするリボイラと、
このリボイラからの蒸気を前記処理槽内へ供給する給蒸管と、
この給蒸管に設けられ、その管路を開閉する給蒸弁と、
この給蒸弁より前記リボイラ側に配置されると共に、前記給蒸弁に近接して前記給蒸管に設けられ、前記給蒸管の内外を連通する開口を有し、前記リボイラからの蒸気の温度に基づき前記開口を閉鎖する排気弁と、
前記処理槽内の空気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、
前記リボイラ内の蒸気圧を検出する蒸気圧検出手段と、
この蒸気圧検出手段の検出信号に基づき、前記ボイラから前記リボイラへの蒸気供給と、前記給蒸弁の開閉の可否とを制御する制御手段と
を備えることを特徴とする蒸気加熱装置。
A treatment tank in which an object to be heated is accommodated;
Reboilers that use steam from the boiler as heat source and soft water or pure water as steam;
A steam supply pipe for supplying steam from the reboiler into the treatment tank;
A steam supply valve that is provided in the steam supply pipe and opens and closes the pipeline;
The steam supply valve is disposed on the reboiler side, is provided in the steam supply pipe in the vicinity of the steam supply valve, and has an opening that communicates the inside and outside of the steam supply pipe. An exhaust valve that closes the opening based on temperature;
Vacuuming means for sucking and discharging the air in the processing tank to the outside, and reducing the pressure in the processing tank;
A vapor pressure detecting means for detecting the vapor pressure in the reboiler;
A steam heating apparatus comprising: control means for controlling supply of steam from the boiler to the reboiler and open / close of the steam supply valve based on a detection signal of the steam pressure detection means.
前記排気弁は、設置箇所の圧力下における飽和蒸気温度より所定温度低い温度で作動する温調トラップとされた
ことを特徴とする請求項1〜3のいずれか1項に記載の蒸気加熱装置。
The steam heating device according to any one of claims 1 to 3, wherein the exhaust valve is a temperature control trap that operates at a temperature lower than a saturated steam temperature under a pressure at an installation location.
前記排気弁は、前記給蒸弁より上流側の前記給蒸管内の温度を検出する管内温度検出手段の検出信号に基づき、設定温度以上で閉鎖するよう制御される開閉弁とされた
ことを特徴とする請求項1〜3のいずれか1項に記載の蒸気加熱装置。
The exhaust valve is an on-off valve that is controlled to close at a set temperature or higher based on a detection signal of a pipe temperature detection means that detects a temperature in the steam supply pipe upstream from the steam supply valve. The steam heating apparatus according to any one of claims 1 to 3.
JP2006098421A 2006-03-31 2006-03-31 Steam-heating apparatus Pending JP2007268017A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019205518A (en) * 2018-05-28 2019-12-05 株式会社マスダックマシナリー Steaming device and heating treatment method
JP7655513B1 (en) 2023-11-06 2025-04-02 丸高工業株式会社 Heating device control method and heating device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019205518A (en) * 2018-05-28 2019-12-05 株式会社マスダックマシナリー Steaming device and heating treatment method
JP7655513B1 (en) 2023-11-06 2025-04-02 丸高工業株式会社 Heating device control method and heating device

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