JP2007229379A - Steam heating apparatus - Google Patents

Steam heating apparatus Download PDF

Info

Publication number
JP2007229379A
JP2007229379A JP2006057948A JP2006057948A JP2007229379A JP 2007229379 A JP2007229379 A JP 2007229379A JP 2006057948 A JP2006057948 A JP 2006057948A JP 2006057948 A JP2006057948 A JP 2006057948A JP 2007229379 A JP2007229379 A JP 2007229379A
Authority
JP
Japan
Prior art keywords
steam
pressure
temperature
operation valve
target value
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2006057948A
Other languages
Japanese (ja)
Inventor
Akira Wakasa
暁 若狭
Taizo Matsukawa
泰三 松川
Shinji Fujii
慎二 藤井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Miura Co Ltd
Miura Protec Co Ltd
Original Assignee
Miura Co Ltd
Miura Protec Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Miura Co Ltd, Miura Protec Co Ltd filed Critical Miura Co Ltd
Priority to JP2006057948A priority Critical patent/JP2007229379A/en
Publication of JP2007229379A publication Critical patent/JP2007229379A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Commercial Cooking Devices (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a steam heating apparatus inexpensively and stably controlling the temperature by preventing hunting of a steam feed operation valve consisting of a solenoid valve. <P>SOLUTION: This steam heating apparatus is provided with a treatment tank 1 storing heating object 7, a steam feed means 2 feeding steam to the treatment tank 1 via the steam feed operation valve 15, and a control means 9 controlling the opening/closing of the steam feed operation valve 15 to retain the pressure in the treatment tank 1 at a target value. The control means 9 converts the changeably set temperature target value to a pressure target value, and controls the opening/closing of the steam feed operation valve 15, which consists of the solenoid valve, based on the detection signal of a pressure sensor 6 and retains the interior of the treatment tank 1 to the pressure target value. The control means 9 varies a difference between an upper limit value and a lower limit value of the pressure when retaining to the pressure target value according to which one of a plurality of preset temperature ranges the temperature target value is pertained. <P>COPYRIGHT: (C)2007,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蒸気調理装置として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 as a steam cooking device for cooking food to be cooked (food or food).

下記特許文献1に開示される蒸煮装置に代表される蒸気加熱装置は、処理槽内へ蒸気を供給して、処理槽内に収容した被加熱物の加熱を図る装置である。このような蒸気加熱装置において、処理槽内の温度調整は、従来、処理槽内の圧力を監視して、処理槽内への蒸気供給(給蒸)と、その供給された蒸気の凝縮を伴う放熱、場合によってはさらに処理槽内からの真空引きによって制御されている。この際、処理槽内への蒸気供給は、その蒸気導入管路に比例制御弁を設け、その開度を調整することが好ましいが、実際にはコスト的な制約から、電磁弁を用いて目標温度に対する上限値と下限値とを設定し、その上下限値間で開閉するオンオフ制御することが多い。
特開平9−266856号公報
A steam heating device typified by a steaming device disclosed in Patent Document 1 below is a device that supplies steam into a processing tank and heats an object to be heated accommodated in the processing tank. In such a steam heating device, the temperature adjustment in the processing tank conventionally involves monitoring the pressure in the processing tank, and supplying steam to the processing tank (steaming) and condensing the supplied steam. It is controlled by heat dissipation and, in some cases, evacuation from the inside of the treatment tank. At this time, it is preferable that the steam supply into the treatment tank is provided with a proportional control valve in the steam introduction pipe and the opening degree thereof is adjusted. In many cases, an upper limit value and a lower limit value for temperature are set, and on / off control is performed to open and close between the upper and lower limit values.
JP-A-9-266856

しかしながら、飽和蒸気温度と飽和蒸気圧力との関係は、同じ温度変化に対して、一定ではない。すなわち、同じ温度差でも、温度が低いほど圧力変化は小さくなり、温度が高いほど圧力変化は大きくなる。そのため、前記電磁弁をオンオフ制御するための上下限値間の差(制御ディファレンシャル)を一定としていると、特に低温域で電磁弁のハンチングが生じ易く、適切な制御がなされないおそれがあった。   However, the relationship between saturated steam temperature and saturated steam pressure is not constant for the same temperature change. That is, even with the same temperature difference, the pressure change decreases as the temperature decreases, and the pressure change increases as the temperature increases. Therefore, if the difference (control differential) between the upper and lower limit values for on / off control of the solenoid valve is constant, hunting of the solenoid valve is likely to occur particularly in a low temperature range, and appropriate control may not be performed.

本発明が解決しようとする課題は、ハンチングを防止した安定な温度制御を安価で行うことのできる蒸気加熱装置を提供することにある。   The problem to be solved by the present invention is to provide a steam heating apparatus capable of performing stable temperature control at a low cost while preventing hunting.

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、給蒸操作弁を介して前記処理槽内へ蒸気供給する給蒸手段と、前記処理槽内の圧力もしくは温度または前記被加熱物の温度を目標値に維持するよう前記給蒸操作弁の開閉を制御する際、前記給蒸操作弁のハンチングの防止を図るハンチング防止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 present invention has been made in order to solve the above-mentioned problems. The invention according to claim 1 is to supply steam into the processing tank through a processing tank in which an object to be heated is accommodated and a steam supply operation valve. When controlling the opening and closing of the steaming operation valve so as to maintain the pressure or temperature in the treatment tank or the temperature of the object to be heated at a target value, prevent the hunting of the steaming operation valve. And a hunting prevention means.

請求項1に記載の発明によれば、給蒸操作弁を電磁弁またはモータバルブから構成しても、ハンチング防止手段により給蒸操作弁のハンチングを防止でき、安価で安定した温度制御を行うことができる。   According to the first aspect of the present invention, even if the steaming operation valve is composed of an electromagnetic valve or a motor valve, hunting of the steaming operation valve can be prevented by the hunting prevention means, and stable temperature control can be performed at low cost. Can do.

請求項2に記載の発明は、前記ハンチング防止手段は、前記目標値に維持する際の圧力または温度について、その上限値と下限値との差を前記目標値に応じて異ならせる手段であ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, the anti-hunting means is means for varying a difference between an upper limit value and a lower limit value in accordance with the target value with respect to the pressure or temperature when maintaining the target value. The steam heating apparatus according to claim 1.

請求項2に記載の発明によれば、目標値に応じて制御ディファレンシャルを変更することで、圧力または温度の維持制御を安価で安定して行うことができる。   According to the second aspect of the invention, the control control of the pressure or temperature can be stably performed at a low cost by changing the control differential according to the target value.

請求項3に記載の発明は、前記処理槽内を減圧する減圧手段と、減圧された前記処置槽内を復圧する復圧手段と、前記処理槽内の蒸気および/または凝縮水を外部へ排出する排出手段と、前記処理槽内の圧力を検出する圧力センサと、前記被加熱物の温度を検出する温度センサと、圧力または温度を前記目標値に維持するように、前記圧力センサまたは前記温度センサの検出信号に基づき前記給蒸操作弁の開閉を制御する制御手段とをさらに備え、この制御手段は、予め定められた複数の圧力範囲または温度範囲のいずれに前記目標値が属するかにより、前記目標値に維持する際の圧力または温度について、その上限値と下限値との差を異ならせる前記ハンチング防止手段を有することを特徴とする請求項2に記載の蒸気加熱装置である。   According to a third aspect of the present invention, there is provided a decompression means for decompressing the inside of the treatment tank, a return pressure means for restoring the decompressed inside of the treatment tank, and discharging steam and / or condensed water from the treatment tank to the outside. Discharging means, a pressure sensor for detecting the pressure in the processing tank, a temperature sensor for detecting the temperature of the object to be heated, and the pressure sensor or the temperature so as to maintain the pressure or temperature at the target value. Control means for controlling the opening and closing of the steaming operation valve based on the detection signal of the sensor, this control means, depending on which of the predetermined pressure range or temperature range the target value belongs, 3. The steam heating apparatus according to claim 2, further comprising: the hunting preventing unit that varies a difference between an upper limit value and a lower limit value of the pressure or temperature when maintaining the target value. 4.

請求項3に記載の発明によれば、予め定められた複数の圧力範囲または温度範囲のいずれに目標値が属するかにより、制御ディファレンシャルを変更することで、圧力または温度の維持制御を安価で安定して簡易に行うことができる。   According to the third aspect of the present invention, the maintenance control of the pressure or temperature can be made inexpensively and stably by changing the control differential depending on which of the plurality of predetermined pressure ranges or temperature ranges the target value belongs to. This can be done easily.

請求項4に記載の発明は、前記上限値と下限値との差は、圧力または温度が低くなる前記範囲ほど大きく設定されることを特徴とする請求項3に記載の蒸気加熱装置である。   The invention according to claim 4 is the steam heating apparatus according to claim 3, wherein the difference between the upper limit value and the lower limit value is set larger as the pressure or temperature becomes lower.

請求項4に記載の発明によれば、飽和蒸気温度と飽和蒸気圧力との関係を考慮して、特に低温域での給蒸操作弁のハンチングを防止することができる。   According to the fourth aspect of the present invention, it is possible to prevent hunting of the steam supply operation valve particularly in a low temperature range in consideration of the relationship between the saturated steam temperature and the saturated steam pressure.

請求項5に記載の発明は、前記制御手段は、変更可能に設定される温度目標値を圧力目標値に換算し、その圧力目標値に前記処理槽内を維持するように、前記圧力センサの検出信号に基づき電磁弁からなる前記給蒸操作弁の開閉を制御するよう構成され、前記ハンチング防止手段は、予め定められた複数の温度範囲のいずれに前記温度目標値が属するかにより、前記圧力目標値に維持する際の圧力の上限値と下限値との差を異ならせることを特徴とする請求項3または請求項4に記載の蒸気加熱装置である。   According to a fifth aspect of the present invention, the control means converts the temperature target value set to be changeable into a pressure target value, and maintains the inside of the processing tank at the pressure target value. The hunting prevention means is configured to control opening and closing of the steam supply operation valve including an electromagnetic valve based on a detection signal, and the hunting preventing means is configured to control the pressure depending on which of the predetermined temperature ranges the temperature target value belongs to The steam heating device according to claim 3 or 4, wherein a difference between an upper limit value and a lower limit value of the pressure when maintaining the target value is made different.

請求項5に記載の発明によれば、目標値を温度で設定しながら、給蒸操作弁の開閉は処理槽内圧力に基づき制御することで、簡易で確実な制御が可能である。   According to the fifth aspect of the present invention, simple and reliable control is possible by controlling the opening and closing of the steam supply operation valve based on the pressure in the processing tank while setting the target value by temperature.

請求項6に記載の発明は、前記給蒸手段は、蒸気発生装置からの蒸気を前記処理槽内へ供給する蒸気導入管路と、この蒸気導入管路の中途に設けられる電磁弁からなる前記給蒸操作弁とを備え、前記ハンチング防止手段は、前記蒸気導入管路に前記電磁弁と順次に設けられるモータバルブを備え、前記電磁弁および前記モータバルブが同時に開閉制御され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 sixth aspect of the present invention, the steam supply means includes the steam introduction pipe that supplies the steam from the steam generator into the processing tank, and the electromagnetic valve provided in the middle of the steam introduction pipe. A steam supply operation valve, and the hunting prevention means includes a motor valve provided sequentially with the electromagnetic valve in the steam introduction pipe, and the electromagnetic valve and the motor valve are controlled to be opened and closed simultaneously. The steam heating apparatus according to claim 1.

請求項6に記載の発明によれば、電磁弁とモータバルブの直列の組合せとし、これらを同時に開閉制御することで、モータバルブの作動時間分の遅れを利用して、給蒸操作弁のハンチングの防止を図ることができる。   According to the sixth aspect of the present invention, a combination of a solenoid valve and a motor valve is used in series, and by simultaneously controlling opening and closing of these, the hunting of the steam supply operation valve is performed using a delay corresponding to the operation time of the motor valve. Can be prevented.

さらに、請求項7に記載の発明は、前記給蒸手段は、蒸気発生装置からの蒸気を前記処理槽内へ供給する蒸気導入管路と、この蒸気導入管路の中途に設けられる電磁弁からなる前記給蒸操作弁とを備え、この給蒸操作弁は、その閉鎖から所定時間内は開放不能とされつつ開閉制御され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。   Further, in the invention according to claim 7, the steam supply means includes a steam introduction pipe for supplying the steam from the steam generator into the processing tank, and an electromagnetic valve provided in the middle of the steam introduction pipe. The steam heating device according to claim 1, wherein the steam supply operation valve is controlled to be opened and closed while being unopenable within a predetermined time from the closing thereof.

請求項7に記載の発明によれば、給蒸操作弁が一旦閉鎖後、再び開放されるまでの最小時間に制限を設けることで、給蒸操作弁のハンチングの防止を図ることができる。   According to the seventh aspect of the present invention, it is possible to prevent hunting of the steaming operation valve by providing a limit on the minimum time until the steaming operation valve is once closed and then opened again.

本発明の蒸気加熱装置によれば、安価で安定した温度制御を行うことができる。   According to the steam heating apparatus of the present invention, it is possible to perform inexpensive and stable temperature control.

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、この処理槽内へ給蒸操作弁を介して蒸気供給する給蒸手段と、前記給蒸操作弁のハンチングの防止を図るハンチング防止手段とを備える。さらに、本実施形態では、処理槽内を減圧する減圧手段と、減圧された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、処理槽内の圧力を検出する圧力センサと、被加熱物の温度を検出する温度センサと、各センサの検出信号などに基づき前記各手段を制御する制御手段とを備える。
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. This steam heating apparatus includes a processing tank in which an object to be heated is stored, a steam supply means for supplying steam to the processing tank via a steaming operation valve, and hunting prevention for preventing hunting of the steaming operation valve. Means. Furthermore, in the present embodiment, a decompression means for decompressing the inside of the treatment tank, a return pressure means for restoring the pressure inside the decompressed treatment tank, a discharge means for discharging the steam and its condensed water to the outside, and a treatment A pressure sensor for detecting the pressure in the tank; a temperature sensor for detecting the temperature of the object to be heated; and a control means for controlling the means based on detection signals of the sensors.

ここで、前記被加熱物は、特に問わないが、たとえば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、蒸気調理装置ということができる。あるいは、前記被加熱物は、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。   Here, although the said to-be-heated material does not ask | require especially, let it be to-be-cooked objects, such as a foodstuff or foodstuff, for example. In this case, the steam heating device can be referred to as a steam cooking device. Alternatively, the object to be heated may be an object to be sterilized such as a scalpel for operation. In this case, the steam heating device can be referred to as a steam sterilization device.

処理槽は、被加熱物を収容可能に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し、その開口部は扉により開閉可能とされる。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、上方へのみ開口する鍋状容器が、その上部開口部を蓋体にて開閉可能に閉じられる構成でもよい。   The treatment tank is a metal can body that is formed in a hollow structure so as to accommodate an object to be heated and is typically formed in a substantially rectangular box shape. This processing tank has a hollow portion that opens to one side surface, and the opening portion can be opened and closed by a door. In a state where the door is closed, the hollow portion is sealed. However, the configuration of the treatment tank is not limited to this, and the pan-like container that opens only upward may be configured such that its upper opening can be closed with a lid.

給蒸手段は、処理槽内へボイラからの蒸気を供給する手段である。この蒸気は、一次ボイラからの蒸気を熱源とする二次ボイラ(リボイラ)にて純水または軟水を加熱して得られる清浄蒸気とするのがよい。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、処理槽への蒸気に混入されるおそれがなく衛生的である。給蒸手段からの蒸気は、蒸気導入管路としての給蒸ラインを介して、処理槽内へ供給される。給蒸ラインの中途に設けた給蒸操作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。   The steam supply means is means for supplying steam from the boiler into the treatment tank. This steam is preferably a clean steam obtained by heating pure water or soft water in a secondary boiler (reboiler) using steam from the primary boiler as a heat source. Thereby, boiler water treatment chemicals, such as rust in piping and a rust preventive agent, are not sanitized and are hygienic. The steam from the steam supply means is supplied into the treatment tank through a steam supply line as a steam introduction conduit. By opening and closing the steaming operation valve provided in the middle of the steaming line, the presence or absence of steam supply to the treatment tank can be switched.

減圧手段は、処理槽内の空気や蒸気を真空引きすることで、処理槽内を減圧する手段である。減圧手段は、真空ポンプ、またはそれに代えてもしくはそれに加えて、蒸気エゼクタまたは水エゼクタなどを備える。減圧手段は、空気導出管路としての減圧ラインを介して、処理槽に接続される。減圧ラインの中途に設けた減圧操作弁を開閉することで、処理槽内からの真空引きの可否が切り替えられる。あるいは、真空ポンプなどの作動の有無を制御することで、処理槽内からの真空引きの可否が切り替えられる。   The decompression means is means for decompressing the inside of the processing tank by evacuating the air or steam in the processing tank. The decompression means includes a vacuum pump or a steam ejector or a water ejector instead of or in addition to the vacuum pump. The decompression means is connected to the treatment tank via a decompression line as an air outlet conduit. By opening and closing a pressure reducing operation valve provided in the middle of the pressure reducing line, whether or not evacuation from the processing tank is possible is switched. Alternatively, by controlling the operation of a vacuum pump or the like, whether or not evacuation can be performed from within the processing tank can be switched.

減圧手段は、さらに熱交換器を備えるのが望ましい。この熱交換器は、処理槽内から吸引した空気中の蒸気を、冷却し凝縮させるものである。この冷却および凝縮作用をなすために、熱交換器には水が供給され、減圧ラインの冷却が図られる。減圧ライン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。   The decompression means preferably further includes a heat exchanger. This heat exchanger cools and condenses the vapor | steam in the air attracted | sucked from the inside of a processing tank. In order to perform this cooling and condensation action, water is supplied to the heat exchanger, and the pressure reduction line is cooled. By preliminarily condensing the vapor in the decompression line with a heat exchanger, it is possible to reduce the load on the subsequent vacuum pump and increase the decompression capability.

復圧手段は、減圧手段により減圧された処理槽内を復圧する手段である。具体的には、減圧された処理槽内へ外気を導入して、処理槽内を大気圧まで復圧することができる。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、空気導入管路としての復圧ラインを介して、処理槽内へ供給される。復圧ラインの中途に設けた復圧操作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 means for returning the pressure in the treatment tank decompressed by the pressure reduction means. Specifically, the outside air can be introduced into the decompressed treatment tank and the pressure inside the treatment tank can be restored to atmospheric pressure. 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 a return pressure line as an air introduction pipe line. By opening and closing a return pressure operation valve provided in the middle of the return pressure line, the presence or absence of introduction of outside air into the processing tank can be switched.

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蒸気導出管路としての排蒸ラインと、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路としての排水ラインとから構成される。ここで、前記排蒸ラインは、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。   The discharge means is means for discharging the steam in the treatment tank and its condensed water to the outside. This discharging means is composed of a steaming line as a steam outlet line for discharging steam from the processing tank and a draining line as a drain line for discharging condensed water from the bottom of the processing tank through a steam trap. Is done. Here, by connecting the steaming line to the bottom of the treatment tank, the condensed water can be discharged in addition to the steam.

処理槽からの排蒸ラインの中途には、排蒸操作弁が設けられる。また、処理槽からの排水ラインの中途には、排水操作弁が設けられる。この排蒸操作弁および/または排水操作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。   A steaming operation valve is provided in the middle of the steaming line from the treatment tank. A drainage operation valve is provided in the middle of the drainage line from the treatment tank. By opening and closing the exhaust steam operation valve and / or the drain operation valve, whether or not steam and / or condensed water is discharged from the processing tank is switched.

ところで、前記減圧操作弁、前記復圧操作弁、前記排蒸操作弁は、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、前記排出手段による処理槽外への排蒸について、その各能力が調整可能となる。また、エゼクタなどの減圧手段自体の減圧能力を調整してもよい。一方、前記給蒸操作弁についても、前記給蒸手段による処理槽内への給蒸能力を調整可能に、開度調整可能とするのが本来好ましいが、コスト面を考慮して本実施形態では、開放または閉鎖のいずれかを択一的に採る電磁弁が使用される。   By the way, it is preferable that the decompression operation valve, the return pressure operation valve, and the exhaust steam operation 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, the return pressure in the treatment tank by the decompression means, and the steaming out of the treatment tank by the discharge means. Further, the pressure reducing capability of the pressure reducing means such as an ejector may be adjusted. On the other hand, for the steaming operation valve, it is originally preferable that the steaming ability into the processing tank by the steaming means can be adjusted, and the opening degree can be adjusted. Solenoid valves that take either open or closed alternatives are used.

制御手段は、給蒸手段、減圧手段、復圧手段、および排出手段などを制御する手段である。逆にいうと、これら各手段は、制御手段により制御され、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。その際、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、処理槽内の被加熱物の温度を検出する温度センサからの検出温度や、経過時間を利用して制御される。   The control means is means for controlling the steam supply means, the decompression means, the decompression means, the discharge means, and the like. Conversely, these means are controlled by the control means, and predetermined operation steps are sequentially executed in accordance with a preset program. In that case, it controls using the detection pressure from the pressure sensor which detects the pressure in a processing tank, the detection temperature from the temperature sensor which detects the temperature of the to-be-heated object in a processing tank, and elapsed time.

典型的には、圧力センサの検出圧力に基づき給蒸操作弁の開閉を制御して、処理槽内の圧力ひいては温度を調整する。そして、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が目標値で設定時間を維持するか、被加熱物の温度が設定温度に達するなど、所望の終了条件が満たされると被加熱物の加熱処理を終了する。   Typically, the opening and closing of the steam supply operation valve is controlled based on the detected pressure of the pressure sensor to adjust the pressure in the processing tank and thus the temperature. Then, a desired end condition is satisfied such that the pressure or temperature in the processing tank or the temperature of the heated object in the processing tank is maintained at the target value for a set time, or the temperature of the heated object reaches the set temperature. And the heat treatment of the object to be heated is completed.

このような加熱処理中、制御手段は、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に、給蒸操作弁の開閉を制御可能である。この際、目標値に対する上限値と下限値とを設定し、その上下限値間で給蒸操作弁の開閉をオンオフ制御する。すなわち、上限値を上回れば給蒸操作弁を閉鎖する一方、下限値を下回れば給蒸操作弁を開放するように、圧力センサまたは温度センサの検出信号に基づき、電磁弁から構成される給蒸操作弁の開閉を制御する。   During such heat treatment, the control means can control the opening and closing of the steam supply operation valve so as to maintain the pressure or temperature in the treatment tank or the temperature of the object to be heated in the treatment tank at the target value. At this time, an upper limit value and a lower limit value with respect to the target value are set, and on / off control of the steam supply operation valve is performed between the upper and lower limit values. That is, the steam supply operation valve is closed when the upper limit value is exceeded, while the steam supply operation valve is opened when the lower limit value is not reached, based on the detection signal of the pressure sensor or temperature sensor. Controls the opening and closing of the operation valve.

ハンチング防止手段は、特に前記目標値への維持制御中、給蒸操作弁のハンチングの防止を図る手段である。このハンチング防止手段の具体的構成は、特に問わないが、たとえば次の三つ実施形態を挙げることができる。   The hunting prevention means is means for preventing hunting of the steaming operation valve, particularly during the maintenance control to the target value. The specific configuration of the hunting prevention means is not particularly limited, and for example, the following three embodiments can be given.

第一実施形態のハンチング防止手段は、目標値に維持する際の圧力または温度について、その上限値と下限値との差(制御ディファレンシャル)を前記目標値に応じて異ならせる手段である。この場合、ハンチング防止手段は、前記制御手段の一部を構成する。そして、ハンチング防止手段は、予め設定された計算式を用いて、温度目標値に対する上限値と下限値とを設定し、給蒸操作弁の開閉を制御する。その際、上限値と下限値との差は、目標値に応じて異なるように、上限値と下限値とを設定する。   The hunting prevention means of the first embodiment is means for varying the difference (control differential) between the upper limit value and the lower limit value of the pressure or temperature when maintaining the target value according to the target value. In this case, the hunting prevention means constitutes a part of the control means. Then, the hunting prevention means sets an upper limit value and a lower limit value with respect to the temperature target value using a preset calculation formula, and controls the opening and closing of the steam supply operation valve. At this time, the upper limit value and the lower limit value are set so that the difference between the upper limit value and the lower limit value varies depending on the target value.

但し、予め定められた複数の圧力範囲または温度範囲のいずれに前記目標値が属するかにより、目標値に維持する際の圧力または温度について、その上限値と下限値との差を異ならせる構成とするのが簡易である。この場合、圧力範囲または温度範囲ごとに、制御ディファレンシャルが対応して予め設定されており、入力または選択された目標値に応じて、その目標値が属する圧力範囲または温度範囲の制御ディファレンシャルと、前記目標値とに基づいて、前記上限値と下限値とが決定される。   However, depending on which of a plurality of predetermined pressure ranges or temperature ranges the target value belongs to, the difference between the upper limit value and the lower limit value of the pressure or temperature when maintaining the target value is different. It is easy to do. In this case, for each pressure range or temperature range, a control differential is set in advance, and according to the target value input or selected, the control differential of the pressure range or temperature range to which the target value belongs, Based on the target value, the upper limit value and the lower limit value are determined.

いずれにしても、飽和蒸気温度と飽和蒸気圧力との関係を考慮して、上限値と下限値との差は、圧力または温度が低くなるほど大きく設定される。つまり、目標温度が高いときには制御ディファレンシャルを小さくし、目標温度が低いときには制御ディファレンシャルを大きくする。これにより、特に低温域での給蒸操作弁のハンチングの防止が図られる。   In any case, in consideration of the relationship between the saturated steam temperature and the saturated steam pressure, the difference between the upper limit value and the lower limit value is set to be larger as the pressure or temperature is lower. That is, when the target temperature is high, the control differential is reduced, and when the target temperature is low, the control differential is increased. Thereby, it is possible to prevent hunting of the steam supply operation valve particularly in a low temperature range.

第二実施形態のハンチング防止手段は、給蒸ラインに前記給蒸操作弁と順次に設けられるモータバルブを備え、給蒸操作弁およびモータバルブを同時に開閉制御する。この場合、給蒸操作弁を構成する電磁弁と直列に、モータバルブが配置されることで、両弁に同時に開放指令を出しても、電磁弁は直ちに開放されるが、モータバルブはその性質上、徐々に開放されることになる。そして、トータルとして、給蒸ラインは徐々に開放されることになる。このようなモータバルブの作動時間分の遅れを利用して、給蒸操作弁のハンチングを防止することができる。   The hunting prevention means of the second embodiment includes a motor valve provided sequentially with the steaming operation valve in the steaming line, and simultaneously controls the opening and closing of the steaming operation valve and the motor valve. In this case, the motor valve is arranged in series with the solenoid valve constituting the steam supply operation valve, so that even if an opening command is issued to both valves at the same time, the solenoid valve is immediately opened. It will be gradually opened up. And as a total, the steam supply line is gradually opened. By utilizing such a delay corresponding to the operating time of the motor valve, it is possible to prevent hunting of the steam supply operation valve.

第三実施形態のハンチング防止手段は、電磁弁から構成される前記給蒸操作弁を、その閉鎖から所定時間内は開放不能としつつ開閉制御する。この場合、ハンチング防止手段は、前記制御手段の一部を構成し、給蒸操作弁が閉鎖されるとタイマーを始動して、その経過時間が所定時間内では給蒸操作弁の開放を阻止する。給蒸操作弁が一旦閉鎖後、再び開放されるまでの最小時間に制限を設けることで、給蒸操作弁のハンチングを防止することができる。   The hunting prevention means of the third embodiment controls the opening and closing of the steaming operation valve composed of an electromagnetic valve while disabling it within a predetermined time from the closing thereof. In this case, the hunting prevention means constitutes a part of the control means, starts a timer when the steaming operation valve is closed, and prevents the steaming operation valve from being opened within a predetermined time. . By setting a limit on the minimum time until the steam supply operation valve is once closed and then opened again, hunting of the steam supply operation valve can be prevented.

上記構成の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。また、加熱工程は、給蒸手段により処理槽内へ蒸気供給して、被加熱物を加熱する工程である。この際、処理槽内へ供給する蒸気により、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、逆に、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。   The operation method of the steam heating apparatus having the above configuration is not particularly limited, but typically, the heating step is performed after the air exclusion step. 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. Moreover, a heating process is a process of supplying a vapor | steam in a processing tank by a steam supply means, and heating a to-be-heated material. At this time, the object to be heated may be heated with the steam supplied into the processing tank while the pressure in the processing tank is higher than the atmospheric pressure. The object to be heated may be heated while being heated.

この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。このような処理中、ハンチング防止手段により、給蒸操作弁のハンチングの防止が図られる。   In this heating step, the pressure or temperature in the treatment tank or the temperature of the object to be heated in the treatment tank is controlled to be maintained at the target value. At this time, the target value may be changed in a plurality of stages. During such processing, hunting of the steaming operation valve is prevented by the hunting prevention means.

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、本発明の蒸気加熱装置の実施例1を示す概略構成図であり、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、本実施例の蒸気加熱装置は、中空構造で開閉可能な処理槽1と、この処理槽1内へ蒸気を供給する給蒸手段2と、処理槽1内の空気や蒸気を外部へ吸引排出して処理槽1内を減圧する減圧手段3と、減圧下の処理槽1内へ外気を導入して復圧する復圧手段4と、処理槽1内の蒸気やその凝縮水を外部へ排出する排出手段5と、処理槽1内の圧力を計測する圧力センサ6と、処理槽1内に収容される被加熱物としての被調理物(食材または食品)7の温度を計測する温度センサ8と、これら各センサ6,8の出力などに基づき前記各手段2,3,4,5を制御する制御手段9とを備える。
Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.
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 steam cooking apparatus. As shown in this figure, the steam heating apparatus of the present embodiment includes a processing tank 1 that can be opened and closed with a hollow structure, steam supply means 2 that supplies steam into the processing tank 1, air in the processing tank 1, Decompression means 3 for reducing the pressure inside the processing tank 1 by sucking and discharging the steam to the outside, return pressure means 4 for returning the pressure by introducing outside air into the processing tank 1 under reduced pressure, steam in the processing tank 1 and its condensation The temperature of the discharge means 5 for discharging water to the outside, the pressure sensor 6 for measuring the pressure in the treatment tank 1, and the cooking object (food or food) 7 as the object to be heated contained in the treatment tank 1 A temperature sensor 8 to be measured and a control means 9 for controlling the means 2, 3, 4 and 5 based on the outputs of the sensors 6 and 8 are provided.

本実施例の処理槽1は、一側面へ開口して中空部を有する処理槽本体10と、この処理槽本体10の開口部を開閉する扉11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11を閉じることで、処理槽本体10の中空部は密閉される。処理槽1内への被調理物7の収容は、処理槽1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1内に棚板12を設けることで対応してもよい。また、被調理物7は、適宜の容器13に入れて、処理槽1内へ収容してもよい。このようにして処理槽1内に収容される被調理物7は、その温度を温度センサ8により計測される。本実施例では、温度センサ8は、被調理物7に差し込まれて、被調理物7の温度を検出する。   The processing tank 1 of the present embodiment is a metal can body that includes a processing tank main body 10 that opens to one side surface and has a hollow portion, and a door 11 that opens and closes the opening of the processing tank main body 10. Since it is such a structure, the hollow part of the processing tank main body 10 is sealed by closing the door 11. The to-be-cooked object 7 may be accommodated in the processing tank 1 via a wagon (not shown) that is taken in and out of the processing tank 1, or a shelf plate 12 is provided in the processing tank 1 as shown in the illustrated example. You may respond by doing. Moreover, the to-be-cooked object 7 may be put in an appropriate container 13 and accommodated in the processing tank 1. Thus, the temperature of the to-be-cooked object 7 accommodated in the processing tank 1 is measured by the temperature sensor 8. In the present embodiment, the temperature sensor 8 is inserted into the cooking object 7 and detects the temperature of the cooking object 7.

処理槽1には、処理槽1内へ蒸気を供給可能に、給蒸手段2が接続される。本実施例の給蒸手段2は、不図示の一次ボイラと二次ボイラ(リボイラ)とを備え、一次ボイラからの蒸気を熱源として、二次ボイラにて軟水を蒸気に変え、そのようにして生成された清浄蒸気を処理槽1内へ供給する。一次ボイラは、通常の一般的なボイラから構成されるが、そのような一次ボイラによる蒸気には、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1内へ供給される蒸気は、直接に被調理物7に接触し得るものである。そこで、二次ボイラにて軟水を蒸気に変えて清浄蒸気を生成し、この清浄蒸気を処理槽1内へ供給する。   A steam supply means 2 is connected to the processing tank 1 so that steam can be supplied into the processing tank 1. The steam supply means 2 of this embodiment includes a primary boiler and a secondary boiler (reboiler) (not shown), uses the steam from the primary boiler as a heat source, changes soft water to steam in the secondary boiler, and so on. The generated clean steam is supplied into the treatment tank 1. Although a primary boiler is comprised from a normal common boiler, there exists a possibility that boiler water treatment chemicals, such as rust in a piping and a rust preventive agent, may mix in the steam by such a primary boiler. However, the steam supplied into the treatment tank 1 can directly come into contact with the object 7 to be cooked. Therefore, clean water is generated by changing soft water to steam in the secondary boiler, and this clean steam is supplied into the treatment tank 1.

二次ボイラからの清浄蒸気は、給蒸ライン14を介して処理槽1内へ供給される。給蒸ライン14の中途には、給蒸操作弁15が設けられている。この給蒸操作弁15は、処理槽1内への給蒸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される。この給蒸操作弁15を開閉操作することで、処理槽1内の圧力ひいては温度を調整できる。但し、処理槽1内の圧力調整は、給蒸操作弁15だけでなく減圧手段3を制御することによっても行うことができる。   Clean steam from the secondary boiler is supplied into the treatment tank 1 via the steam supply line 14. A steam supply operation valve 15 is provided in the middle of the steam supply line 14. This steam supply operation valve 15 is sufficient if it can be configured to switch the presence or absence of steam supply into the treatment tank 1, and is configured by an electromagnetic valve that cannot be adjusted in opening degree and takes either an open state or a closed state. . By opening and closing the steam supply operation valve 15, the pressure in the processing tank 1 and thus the temperature can be adjusted. However, the pressure in the treatment tank 1 can be adjusted by controlling not only the steam supply operation valve 15 but also the decompression means 3.

処理槽1には、処理槽1内の空気や蒸気を外部へ真空引きして、処理槽1内を減圧する減圧手段3が接続される。本実施例では、減圧ライン16を介して処理槽1には、減圧操作弁17、熱交換器18、逆止弁19、さらには水封式真空ポンプ20が順次に接続される。本実施例の減圧操作弁17は、比例制御弁またはモータバルブなどの開度調整可能な構成である。   The processing tank 1 is connected to a decompression means 3 that evacuates the air and steam in the processing tank 1 to decompress the processing tank 1. In this embodiment, a pressure reducing operation valve 17, a heat exchanger 18, a check valve 19, and a water ring vacuum pump 20 are sequentially connected to the processing tank 1 through the pressure reducing line 16. The pressure reducing operation valve 17 of the present embodiment has a configuration capable of adjusting the opening, such as a proportional control valve or a motor valve.

真空ポンプ20には、封水給水弁21を介して水が供給され、真空ポンプ20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21は、真空ポンプ20に連動して開かれる。また、熱交換器18にも、熱交給水弁22を介して冷却用の水が供給され、排水口へ排水される。熱交換器18に冷却水が供給されることで、減圧ライン16中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 20 via a sealed water supply valve 21, and the waste water from the vacuum pump 20 is discharged to a drain port (not shown). The sealed water supply valve 21 is opened in conjunction with the vacuum pump 20. In addition, cooling water is also supplied to the heat exchanger 18 through the heat exchange water supply valve 22 and drained to the drain outlet. By supplying the cooling water to the heat exchanger 18, the steam in the decompression line 16 can be cooled and condensed.

処理槽1には、減圧手段3にて減圧された後、復圧するための復圧手段4が接続されている。本実施例の復圧手段4は、処理槽1に接続された復圧ライン23が、除菌フィルター24を介して外気と連通可能に設けられている。この復圧ライン23の中途には、復圧操作弁25が開閉可能に設けられており、この復圧操作弁25の開放により、処理槽1内は大気圧に開放可能とされる。   The treatment tank 1 is connected to a decompression means 4 for decompressing after being decompressed by the decompression means 3. The return pressure means 4 of the present embodiment is provided with a return pressure line 23 connected to the processing tank 1 so as to be able to communicate with the outside air via a sterilization filter 24. In the middle of the return pressure line 23, a return pressure operation valve 25 is provided so as to be openable and closable. By opening the return pressure operation valve 25, the inside of the processing tank 1 can be opened to atmospheric pressure.

処理槽1には、処理槽1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5が接続されている。この排出手段5は、処理槽1内の蒸気や空気を外部へ排出するための排蒸手段26と、処理槽1内に生じた凝縮水を外部へ排出するための排水手段27とに分けられる。   The treatment tank 1 is connected to a discharge means 5 for discharging the steam in the treatment tank 1 and its condensed water to the outside. The discharging means 5 is divided into a steaming means 26 for discharging steam and air in the processing tank 1 to the outside, and a draining means 27 for discharging condensed water generated in the processing tank 1 to the outside. .

排蒸手段26は、排蒸ライン28を介して処理槽1内の空気や蒸気を処理槽1外へ導出する手段である。排蒸ライン28の中途には、比例制御弁またはモータバルブなどの開度調整可能な排蒸操作弁29が設けられる。図示例では、処理槽1の下部に排蒸ライン28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1の上部にも同様の排蒸ライン(不図示)を設けることができる。処理槽1の下部からの排蒸ライン28は、処理槽1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 26 is a means for leading the air and steam in the processing tank 1 out of the processing tank 1 through the steaming line 28. In the middle of the steaming line 28, a steaming control valve 29 such as a proportional control valve or a motor valve whose opening degree can be adjusted is provided. In the illustrated example, the exhaust steam line 28 is connected to the lower part of the treatment tank 1, but instead of this, or in addition to this, a similar exhaust steam line (not shown) is also provided at the upper part of the treatment tank 1. Can do. The steaming line 28 from the lower part of the processing tank 1 can also be used for discharging condensed water accumulated in the lower part of the processing tank 1 to the outside.

一方、排水手段27は、スチームトラップ30を有する排水ライン31からなり、この排水ライン31を介して処理槽1内の底部に溜まる凝縮水は、処理槽1外へ排水可能とされる。そして、この排水ライン31の中途には、電磁弁から構成される排水操作弁32が設けられる。   On the other hand, the drainage means 27 includes a drainage line 31 having a steam trap 30, and the condensed water accumulated at the bottom of the treatment tank 1 through the drainage line 31 can be drained out of the treatment tank 1. And in the middle of this drainage line 31, the drainage operation valve 32 comprised from an electromagnetic valve is provided.

さらに、処理槽1には、圧力センサ6が設けられる。この圧力センサ6により、処理槽1内の圧力が検出される。但し、圧力センサ6に代えて、温度センサ(不図示)を利用することも可能である。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できる。   Furthermore, the processing tank 1 is provided with a pressure sensor 6. The pressure in the processing tank 1 is detected by the pressure sensor 6. However, it is also possible to use a temperature sensor (not shown) instead of the pressure sensor 6. Any sensor can be used by converting pressure and temperature.

前記給蒸手段2、前記減圧手段3、前記復圧手段4、前記排出手段5などは、制御手段9により制御される。この制御手段9は、それが把握する経過時間や前記圧力センサ6および前記温度センサ8からの検出信号などに基づいて、前記各手段2,3,4,5を制御する制御器33である。具体的には、給蒸操作弁15、減圧操作弁17、真空ポンプ20、封水給水弁21、熱交給水弁22、復圧操作弁25、排蒸操作弁29、排水操作弁32、圧力センサ6および温度センサ8などは、制御器33に接続される。そして、制御器33は、所定の手順(プログラム)に従い、処理槽1内の被調理物7の加熱調理を行う。   The steam supply means 2, the decompression means 3, the return pressure means 4, the discharge means 5 and the like are controlled by a control means 9. The control means 9 is a controller 33 for controlling the means 2, 3, 4 and 5 based on the elapsed time grasped by the control means 9 and detection signals from the pressure sensor 6 and the temperature sensor 8. Specifically, the steam supply operation valve 15, the pressure reduction operation valve 17, the vacuum pump 20, the sealed water supply valve 21, the heat exchange water supply valve 22, the return pressure operation valve 25, the steaming operation valve 29, the drain operation valve 32, the pressure The sensor 6 and the temperature sensor 8 are connected to the controller 33. And the controller 33 performs the cooking of the to-be-cooked thing 7 in the processing tank 1 according to a predetermined procedure (program).

本実施例では、制御器33は、圧力センサ6の検出圧力に基づき、処理槽1内の圧力が目標値に維持されるように、給蒸操作弁15の開閉を制御可能である。ここで、目標値は、設定器34により変更可能に制御器33へ設定される。その際、圧力目標値として設定するよう構成してもよいし、温度目標値として設定するよう構成してもよい。温度目標値で設定する場合、制御器33は圧力に換算して処理する。いずれにしても、制御器33は、処理槽1内を圧力目標値に維持するために、その目標値に対する上限値と下限値とを設定する。   In the present embodiment, the controller 33 can control the opening and closing of the steam supply operation valve 15 based on the pressure detected by the pressure sensor 6 so that the pressure in the processing tank 1 is maintained at the target value. Here, the target value is set in the controller 33 so as to be changeable by the setting unit 34. At that time, the pressure target value may be set, or the temperature target value may be set. When setting with a temperature target value, the controller 33 converts into pressure and processes. In any case, the controller 33 sets an upper limit value and a lower limit value for the target value in order to maintain the inside of the processing tank 1 at the pressure target value.

その際、制御器33の一部として組み込まれたハンチング防止手段により、上限値と下限値との差(制御ディファレンシャル)が、目標値に応じて変更される。たとえば、三つの温度範囲に分けて制御ディファレンシャルを設定しておき、設定器34により設定される温度目標値とそれが属する制御ディファレンシャルとに基づいて、その目標値に維持する際の圧力目標値の上限値と下限値とが設定される。   At that time, the difference (control differential) between the upper limit value and the lower limit value is changed according to the target value by the hunting prevention means incorporated as a part of the controller 33. For example, the control differential is set in three temperature ranges, and based on the temperature target value set by the setting device 34 and the control differential to which it belongs, the pressure target value for maintaining the target value is set. An upper limit value and a lower limit value are set.

そして、制御器33は、上限値を上回れば給蒸操作弁15を閉鎖する一方、下限値を下回れば給蒸操作弁15を開放することで、処理槽1内の圧力を目標値に維持する。ところで、飽和蒸気温度と飽和蒸気圧力との関係を考慮して、圧力または温度が低くなる前記温度範囲ほど、制御ディファレンシャルは大きく設定される。その理由は、飽和蒸気温度−圧力特性曲線の圧力に対する温度の変化勾配が圧力が高くなるに従って小さくなる特性となっているので、圧力(温度)が低い領域と高い領域とで同じディファレンシャルに設定すると、圧力(温度)の低い領域では少しの圧力変動により給蒸操作弁が開閉してしまうことによる。この実施例1では、圧力または温度が低くなる前記温度範囲ほど、制御ディファレンシャルは大きく設定しているので、給蒸操作弁15のハンチングを防止しつつ、給蒸操作弁15の開閉が制御される。   Then, the controller 33 closes the steam supply operation valve 15 if the upper limit value is exceeded, while maintaining the pressure in the processing tank 1 at the target value by opening the steam supply operation valve 15 if it falls below the lower limit value. . By the way, in consideration of the relationship between the saturated steam temperature and the saturated steam pressure, the control differential is set to be larger in the temperature range where the pressure or the temperature becomes lower. The reason is that the temperature change gradient with respect to the pressure of the saturated steam temperature-pressure characteristic curve becomes smaller as the pressure increases, so if the same differential is set in the low pressure region and high pressure region This is because, in a region where the pressure (temperature) is low, the steam supply operation valve opens and closes due to slight pressure fluctuations. In the first embodiment, since the control differential is set to be larger in the temperature range where the pressure or temperature is lower, the opening / closing of the steam supply operation valve 15 is controlled while preventing the hunting of the steam supply operation valve 15. .

蒸気加熱装置の使用に際しては、加熱調理しようとする被調理物7を処理槽1内に収容し、処理槽1の扉11を閉じる。この初期状態では、給蒸操作弁15、減圧操作弁17、封水給水弁21、熱交給水弁22は閉じられ、真空ポンプ20は作動を停止した状態で、復圧操作弁25と排蒸操作弁29および排水操作弁32は開かれる。そして、この状態から、典型的には、空気排除工程と加熱工程とが順次に行われる。   When using the steam heating device, the object 7 to be cooked is accommodated in the processing tank 1 and the door 11 of the processing tank 1 is closed. In this initial state, the steam supply operation valve 15, the pressure reducing operation valve 17, the sealed water supply valve 21, and the heat exchange water supply valve 22 are closed, and the vacuum pump 20 is stopped in operation, and the return pressure operation valve 25 and the exhaust steam control valve are stopped. The operation valve 29 and the drain operation valve 32 are opened. And from this state, typically, an air exclusion process and a heating process are sequentially performed.

空気排除工程では、給蒸操作弁15、復圧操作弁25、排蒸操作弁29および排水操作弁32を閉じた状態で、減圧手段3を作動させる。但し、ここでは熱交換器18は機能させずに、真空ポンプ20のみを作動させて処理槽1内を減圧する。すなわち、熱交給水弁22を閉じた状態で、減圧操作弁17および封水給水弁21を開いて真空ポンプ20を作動させる。このようにして、処理槽1内の空気を減圧手段3により外部へ真空引きして、処理槽1内の空気を排除することで、後の加熱工程における被調理物7の加熱調理を効果的に行うことができる。   In the air exclusion process, the decompression means 3 is operated with the steam supply operation valve 15, the return pressure operation valve 25, the exhaust steam operation valve 29 and the drain operation valve 32 closed. However, here, the heat exchanger 18 is not functioned, and only the vacuum pump 20 is operated to depressurize the inside of the processing tank 1. That is, with the heat exchange water supply valve 22 closed, the pressure reducing operation valve 17 and the sealed water supply valve 21 are opened to operate the vacuum pump 20. In this way, the air in the processing tank 1 is evacuated to the outside by the decompression means 3 and the air in the processing tank 1 is eliminated, thereby effectively cooking the cooking object 7 in the subsequent heating step. Can be done.

このような処理槽1内からの空気排除は、圧力センサ6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。さらに、この空気排除工程は、給蒸操作弁15を開いた状態で処理槽1内へ蒸気供給して行うこともできる。また、この空気排除工程は、必要により省略することもできる。   Such air exclusion from the processing tank 1 may be performed up to a set pressure by using the pressure sensor 6 or may be performed only for a set time. Furthermore, this air exclusion process can also be performed by supplying steam into the treatment tank 1 with the steam supply operation valve 15 opened. Further, this air exclusion step can be omitted if necessary.

加熱工程では、処理槽1内へ蒸気供給して、処理槽1内の被調理物7を加熱調理する工程である。具体的には、減圧操作弁17、封水給水弁21、熱交給水弁22、復圧操作弁25、排蒸操作弁29を閉じると共に、真空ポンプ20の作動を停止した状態で、給蒸操作弁15を開いて処理槽1内へ蒸気供給する。この際、処理槽1内が大気圧を超える場合、排水操作弁32を開くことで、処理槽1内の底部から凝縮水を外部へ排出する。   In the heating process, steam is supplied into the processing tank 1 to cook the cooking object 7 in the processing tank 1. Specifically, the depressurization operation valve 17, the sealed water supply valve 21, the heat exchange water supply valve 22, the return pressure operation valve 25, and the exhaust steam operation valve 29 are closed and the operation of the vacuum pump 20 is stopped. The operation valve 15 is opened to supply steam into the treatment tank 1. At this time, when the inside of the treatment tank 1 exceeds the atmospheric pressure, the drainage operation valve 32 is opened to discharge condensed water from the bottom of the treatment tank 1 to the outside.

このようにして、処理槽1内が所望の設定圧力になるまで、給蒸手段2により処理槽1内へ蒸気供給される。そして、処理槽1内を設定圧力に保持するように、圧力センサ6の検出圧力に基づき給蒸手段2による処理槽1内への蒸気供給を調整して、処理槽1内の被調理物7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 1 by the steam supply means 2 until the inside of the processing tank 1 reaches a desired set pressure. And the steam supply to the processing tank 1 by the steam supply means 2 is adjusted based on the detected pressure of the pressure sensor 6 so as to keep the inside of the processing tank 1 at the set pressure, and the cooked object 7 in the processing tank 1 Is cooked. During this heating process, the set pressure may be changed up and down stepwise.

ところで、処理槽1内へ蒸気供給して行う被調理物7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3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 food 7 to be cooked by supplying steam into the treatment tank 1 is pressureless cooking performed at atmospheric pressure, pressure cooking performed at a pressure exceeding atmospheric pressure, and the decompression means 3 is operated when desired. And steaming under reduced pressure at a pressure lower than atmospheric pressure.

無圧蒸煮の場合、減圧操作弁17、封水給水弁21、熱交給水弁22、復圧操作弁25を閉じると共に、真空ポンプ20の作動を停止した状態で、給蒸操作弁15、排蒸操作弁29、排水操作弁32を開いて、処理槽1内へ蒸気を供給する。   In the case of non-pressure steaming, the pressure reducing operation valve 17, the sealed water supply valve 21, the heat exchange water supply valve 22, and the return pressure operation valve 25 are closed and the operation of the vacuum pump 20 is stopped, The steam operation valve 29 and the drain operation valve 32 are opened, and steam is supplied into the treatment tank 1.

加圧蒸煮の場合、減圧操作弁17、封水給水弁21、熱交給水弁22、復圧操作弁25、排蒸操作弁29を閉じると共に、真空ポンプ20の作動を停止した状態で、給蒸操作弁15、排水操作弁32を開いて、処理槽1内へ蒸気を供給する。従って、加圧蒸煮の場合には、排水ライン31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 depressurization operation valve 17, the sealed water supply valve 21, the heat exchange water supply valve 22, the return pressure operation valve 25, and the exhaust steam operation valve 29 are closed and the operation of the vacuum pump 20 is stopped. The steam operation valve 15 and the drain operation valve 32 are opened to supply steam into the treatment tank 1. Therefore, in the case of pressurized steaming, the condensed water is automatically discharged from the drain line 31 to the outside.

減圧蒸煮の場合は、復圧操作弁25、排蒸操作弁29、排水操作弁32を閉じた状態で、給蒸操作弁15を開いて、処理槽1内へ蒸気を供給する。この際、処理槽1内が設定上限圧力を超えると、減圧手段3を作動させて、設定下限圧力まで処理槽1内を減圧する。すなわち、減圧操作弁17、封水給水弁21、熱交給水弁22を開いた状態で、真空ポンプ20を作動させて、設定下限圧力まで処理槽1内を減圧し、設定下限圧力になると、これら各弁17,21,22を閉じると共に真空ポンプ20の作動を停止する。   In the case of steaming under reduced pressure, the steam supply operation valve 15 is opened and the steam is supplied into the treatment tank 1 with the decompression operation valve 25, the exhaust steam operation valve 29, and the drain operation valve 32 closed. At this time, when the inside of the processing tank 1 exceeds the set upper limit pressure, the decompression means 3 is operated to decompress the inside of the processing tank 1 to the set lower limit pressure. That is, when the pressure reducing operation valve 17, the sealed water supply valve 21, and the heat exchange water supply valve 22 are opened, the vacuum pump 20 is operated to depressurize the inside of the treatment tank 1 to the set lower limit pressure. The valves 17, 21, 22 are closed and the operation of the vacuum pump 20 is stopped.

いずれの場合も、基本的には、蒸気供給による処理槽1内の加圧要因と、供給された蒸気の凝縮による処理槽1内の減圧要因とがバランスを保つように、給蒸操作弁15を開閉制御して、処理槽1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3を作動させる場合がある。このような圧力目標値での維持制御中には、前述したように、ハンチング防止手段により、給蒸操作弁15のハンチングが防止される。   In any case, basically, the steam supply operation valve 15 is maintained so that the pressurization factor in the treatment tank 1 by the supply of steam and the decompression factor in the treatment tank 1 by the condensation of the supplied steam are kept in balance. Is heated and cooked while maintaining the pressure in the treatment tank 1 at the target value. However, in the case of reduced-pressure steaming, if the set upper limit pressure is exceeded, the decompression means 3 may be operated as described above. During maintenance control at such a pressure target value, as described above, hunting of the steam supply operation valve 15 is prevented by the hunting prevention means.

このようにして、加熱工程では、処理槽1内へ蒸気が供給されることで、処理槽1内に収容された被調理物7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1内へ供給される蒸気は、二次ボイラ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7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 step, the cooking object 7 accommodated in the processing tank 1 can be cooked by supplying steam into the processing tank 1. At this time, as described above, the steam supplied into the processing tank 1 is clean steam generated from soft water in the secondary boiler. Therefore, safe and reliable cooking can be realized. Moreover, uniform heating dishes are made in a short time by spreading clean steam around the entire periphery of the object 7 to be cooked.

加熱工程では、処理槽1内への蒸気供給により処理槽1内の圧力を調整することで、処理槽1内の温度を調整することができる。本実施例では、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1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 1 can be adjusted by adjusting the pressure in the processing tank 1 by supplying steam into the processing tank 1. In the present embodiment, cooking is possible by setting the temperature freely 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 1.

そして、加熱工程の終了時には、給蒸操作弁15が閉じられる。その際、処理槽1内が大気圧を超える圧力であれば、排蒸操作弁29を開いて、処理槽1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1内が大気圧未満であれば、減圧手段3および排出手段5を作動させず、かつ、給蒸操作弁15を閉じると共に復圧操作弁25を開いて、処理槽1内を大気圧まで復圧する。   At the end of the heating process, the steam supply operation valve 15 is closed. At that time, if the pressure inside the treatment tank 1 exceeds atmospheric pressure, the exhaust steam operation valve 29 is opened, and drainage and steam exhaust are performed until the inside of the treatment tank 1 reaches atmospheric pressure. On the other hand, if the inside of the treatment tank 1 is less than the atmospheric pressure, the decompression means 3 and the discharge means 5 are not operated, and the steam supply operation valve 15 is closed and the return pressure operation valve 25 is opened. Restore pressure to atmospheric pressure.

図2は、本発明の蒸気加熱装置の実施例2を示す概略構成図であり、蒸気調理装置に適用した例を示している。本実施例2の蒸気加熱装置も、基本的には前記実施例1と同様の構成である。そこで、以下では、両者の異なる点を中心に説明し、対応する箇所には同一の符号を付して説明する。   FIG. 2: is a schematic block diagram which shows Example 2 of the steam heating apparatus of this invention, and has shown the example applied to the steam cooking apparatus. The steam heating apparatus according to the second embodiment is basically configured in the same manner as the first embodiment. Therefore, in the following description, the differences between the two will be mainly described, and corresponding portions will be described with the same reference numerals.

前記実施例1では、温度目標値に応じて制御ディファレンシャルを変更することで、給蒸操作弁15のハンチングの防止を図る構成としたが、本実施例2では、これに代えてまたはこれに加えて、給蒸ライン14にモータバルブ35を設けることでハンチングを抑制する。すなわち、本実施例2では、給蒸ライン14には、電磁弁からなる給蒸操作弁15の他に、モータバルブ35が直列に接続されている。図示例では、ボイラ(不図示)の側から順に、モータバルブ35と給蒸操作弁15とを設けたが、給蒸操作弁15とモータバルブ35との順序は入替可能である。   In the first embodiment, the control differential is changed according to the temperature target value to prevent hunting of the steam supply operation valve 15. However, in the second embodiment, instead of or in addition to this, Thus, hunting is suppressed by providing a motor valve 35 in the steam supply line 14. That is, in the second embodiment, the steam supply line 14 is connected with a motor valve 35 in series in addition to the steam supply operation valve 15 formed of an electromagnetic valve. In the illustrated example, the motor valve 35 and the steam supply operation valve 15 are provided in this order from the boiler (not shown) side, but the order of the steam supply operation valve 15 and the motor valve 35 can be interchanged.

本実施例2の場合、制御器33は、給蒸操作弁15およびモータバルブ35を同時に開閉制御する。給蒸操作弁15を構成する電磁弁と直列に、モータバルブ35が配置されるが、両弁15,35に同時に開放指令を出しても、電磁弁15は直ちに開放されるものの、モータバルブ35はその性質上、徐々に開度を増すように開放されることになる。このようなモータバルブ35の作動時間分の遅れを利用して、給蒸操作弁15のハンチングの防止を図ることができる。   In the case of the second embodiment, the controller 33 controls opening / closing of the steam supply operation valve 15 and the motor valve 35 simultaneously. Although the motor valve 35 is arranged in series with the electromagnetic valve constituting the steam supply operation valve 15, the motor valve 35 is immediately opened even if an opening command is issued simultaneously to both valves 15, 35, but the motor valve 35 is opened. Due to its nature, it is opened to gradually increase the opening. By utilizing such a delay for the operation time of the motor valve 35, it is possible to prevent hunting of the steam supply operation valve 15.

本発明の蒸気加熱装置は、前記各実施例の構成に限らず適宜変更可能である。たとえば、前記各実施例では、減圧手段3として、熱交換器18と真空ポンプ20との組合せを用いたが、蒸気エゼクタ、水エゼクタ、缶体冷却(冷却水による処理槽壁の冷却)、または凝縮熱交換器などを、単独または組み合わせて利用してもよい。また、前記加熱工程後には、所望により、含浸工程または真空冷却工程を行ってもよい。   The steam heating apparatus of the present invention is not limited to the configuration of each of the above embodiments, and can be changed as appropriate. For example, in each of the above-described embodiments, the combination of the heat exchanger 18 and the vacuum pump 20 is used as the decompression unit 3, but a steam ejector, a water ejector, can cooling (cooling of a processing tank wall with cooling water), or A condensation heat exchanger or the like may be used alone or in combination. Further, after the heating step, an impregnation step or a vacuum cooling step may be performed as desired.

また、処理槽1内を設定圧力に維持する際の給蒸操作弁15のハンチング防止手段も前記各実施例の構成に限定されない。たとえば、前記実施例1において、電磁弁から構成される給蒸操作弁15を、その閉鎖から所定時間内は開放不能としつつ開閉制御することで、給蒸操作弁15のハンチングの防止を図ってもよい。この場合、ハンチング防止手段は、前記制御器33の一部を構成し、給蒸操作弁15が閉鎖されるとタイマーを始動して、その経過時間が所定時間内では給蒸操作弁15の開放を制限する。給蒸操作弁15が一旦閉鎖後、再び開放されるまでの最小時間に制限を設けることで、給蒸操作弁15のハンチングの防止を図ることができる。   Further, the hunting prevention means of the steam supply operation valve 15 when the inside of the processing tank 1 is maintained at the set pressure is not limited to the configuration of each of the above embodiments. For example, in the first embodiment, hunting of the steam supply operation valve 15 is prevented by opening / closing the steam supply operation valve 15 including a solenoid valve while making the steam supply operation valve 15 impossible to open within a predetermined time from the closing thereof. Also good. In this case, the hunting prevention means constitutes a part of the controller 33, starts a timer when the steaming operation valve 15 is closed, and opens the steaming operation valve 15 within a predetermined time. Limit. By providing a restriction on the minimum time until the steam supply operation valve 15 is once opened after being closed, hunting of the steam supply operation valve 15 can be prevented.

さらに、前記各実施例では、処理槽1内の圧力を目標値に維持するように、圧力センサ6の検出圧力に基づき給蒸操作弁15を開閉制御したが、処理槽1内の温度を目標値に維持するように、処理槽1内の温度を検出する温度センサ(不図示)の検出温度に基づき、給蒸操作弁15を開閉制御してもよい。あるいは、処理槽1内に収容した被調理物7の温度を目標値に維持するように、被調理物7の温度を検出する温度センサ8の検出温度に基づき、給蒸操作弁15を開閉制御してもよい。   Furthermore, in each said Example, although the steam supply operation valve 15 was controlled to open and close based on the detection pressure of the pressure sensor 6 so that the pressure in the processing tank 1 might be maintained at a target value, the temperature in the processing tank 1 is set as a target. The steam supply operation valve 15 may be controlled to open and close based on the temperature detected by a temperature sensor (not shown) that detects the temperature in the processing tank 1 so as to maintain the value. Or based on the detected temperature of the temperature sensor 8 which detects the temperature of the to-be-cooked item 7 so that the temperature of the to-be-cooked item 7 accommodated in the processing tank 1 may be maintained at a target value, the steam supply operation valve 15 is controlled to open and close. May be.

また、前記各実施例では、食材や食品などの被調理物7を、処理槽1内に収容してその加熱調理を図る蒸気調理装置について説明したが、手術用メスなどの被滅菌物(不図示)を、処理槽1内に収容してその滅菌処理を図る蒸気滅菌装置にも同様に適用可能である。   Further, in each of the above-described embodiments, the steam cooking apparatus that accommodates the cooking object 7 such as food and food in the processing tank 1 and heats the cooking object has been described. Can be similarly applied to a steam sterilization apparatus which accommodates the gas in the treatment tank 1 and performs sterilization.

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る。It is a schematic block diagram which shows Example 1 of the steam heating apparatus of this invention. 本発明の蒸気加熱装置の実施例2を示す概略構成図である。It is a schematic block diagram which shows Example 2 of the steam heating apparatus of this invention.

符号の説明Explanation of symbols

1 処理槽
2 給蒸手段
3 減圧手段
4 復圧手段
5 排出手段
6 圧力センサ
7 被加熱物(被調理物)
8 温度センサ
9 制御手段
14 給蒸ライン(蒸気導入管路)
15 給蒸操作弁(電磁弁)
35 モータバルブ
DESCRIPTION OF SYMBOLS 1 Processing tank 2 Steaming means 3 Pressure reducing means 4 Pressure-reducing means 5 Discharge means 6 Pressure sensor 7 Object to be heated (cooking object)
8 Temperature sensor 9 Control means 14 Steaming line (steam introduction line)
15 Steaming operation valve (solenoid valve)
35 Motor valve

Claims (7)

被加熱物が収容される処理槽と、
給蒸操作弁を介して前記処理槽内へ蒸気供給する給蒸手段と、
前記処理槽内の圧力もしくは温度または前記被加熱物の温度を目標値に維持するよう前記給蒸操作弁の開閉を制御する際、前記給蒸操作弁のハンチングの防止を図るハンチング防止手段と
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;
Steaming means for supplying steam into the treatment tank via a steaming operation valve;
Anti-hunting means for preventing hunting of the steaming operation valve when controlling the opening and closing of the steaming operation valve so as to maintain the pressure or temperature in the processing tank or the temperature of the object to be heated at a target value. A steam heating apparatus comprising:
前記ハンチング防止手段は、前記目標値に維持する際の圧力または温度について、その上限値と下限値との差を前記目標値に応じて異ならせる手段である
ことを特徴とする請求項1に記載の蒸気加熱装置。
The said hunting prevention means is a means which makes the difference of the upper limit value and lower limit value differ according to the said target value about the pressure or temperature at the time of maintaining to the said target value. Steam heating device.
前記処理槽内を減圧する減圧手段と、
減圧された前記処置槽内を復圧する復圧手段と、
前記処理槽内の蒸気および/または凝縮水を外部へ排出する排出手段と、
前記処理槽内の圧力を検出する圧力センサと、
前記被加熱物の温度を検出する温度センサと、
圧力または温度を前記目標値に維持するように、前記圧力センサまたは前記温度センサの検出信号に基づき前記給蒸操作弁の開閉を制御する制御手段とをさらに備え、
この制御手段は、予め定められた複数の圧力範囲または温度範囲のいずれに前記目標値が属するかにより、前記目標値に維持する際の圧力または温度について、その上限値と下限値との差を異ならせる前記ハンチング防止手段を有する
ことを特徴とする請求項2に記載の蒸気加熱装置。
Decompression means for decompressing the inside of the treatment tank;
Return pressure means for returning pressure in the reduced pressure treatment tank;
Discharging means for discharging steam and / or condensed water in the treatment tank to the outside;
A pressure sensor for detecting the pressure in the processing tank;
A temperature sensor for detecting the temperature of the object to be heated;
Control means for controlling opening and closing of the steaming operation valve based on a detection signal of the pressure sensor or the temperature sensor so as to maintain the pressure or temperature at the target value;
The control means determines the difference between the upper limit value and the lower limit value for the pressure or temperature when maintaining the target value, depending on which of the predetermined pressure range or temperature range the target value belongs to. The steam heating apparatus according to claim 2, further comprising the hunting prevention unit that makes the difference.
前記上限値と下限値との差は、圧力または温度が低くなる前記範囲ほど大きく設定される
ことを特徴とする請求項3に記載の蒸気加熱装置。
The steam heating device according to claim 3, wherein the difference between the upper limit value and the lower limit value is set to be larger as the pressure or temperature becomes lower.
前記制御手段は、変更可能に設定される温度目標値を圧力目標値に換算し、その圧力目標値に前記処理槽内を維持するように、前記圧力センサの検出信号に基づき電磁弁からなる前記給蒸操作弁の開閉を制御するよう構成され、
前記ハンチング防止手段は、予め定められた複数の温度範囲のいずれに前記温度目標値が属するかにより、前記圧力目標値に維持する際の圧力の上限値と下限値との差を異ならせる
ことを特徴とする請求項3または請求項4に記載の蒸気加熱装置。
The control means converts the temperature target value set so as to be changeable into a pressure target value, and maintains the inside of the processing tank at the pressure target value based on the detection signal of the pressure sensor. Configured to control the opening and closing of the steaming operation valve,
The hunting prevention means varies the difference between the upper limit value and the lower limit value of the pressure when maintaining the pressure target value depending on which of the predetermined temperature ranges the temperature target value belongs to. The steam heating apparatus according to claim 3 or 4, wherein the steam heating apparatus is characterized.
前記給蒸手段は、蒸気発生装置からの蒸気を前記処理槽内へ供給する蒸気導入管路と、この蒸気導入管路の中途に設けられる電磁弁からなる前記給蒸操作弁とを備え、
前記ハンチング防止手段は、前記蒸気導入管路に前記電磁弁と順次に設けられるモータバルブを備え、
前記電磁弁および前記モータバルブが同時に開閉制御される
ことを特徴とする請求項1に記載の蒸気加熱装置。
The steam supply means includes a steam introduction pipe for supplying steam from a steam generator into the processing tank, and the steam supply operation valve including an electromagnetic valve provided in the middle of the steam introduction pipe,
The hunting prevention means includes a motor valve provided in sequence with the electromagnetic valve in the steam introduction pipe line,
The steam heating apparatus according to claim 1, wherein the electromagnetic valve and the motor valve are controlled to be opened and closed simultaneously.
前記給蒸手段は、蒸気発生装置からの蒸気を前記処理槽内へ供給する蒸気導入管路と、この蒸気導入管路の中途に設けられる電磁弁からなる前記給蒸操作弁とを備え、
この給蒸操作弁は、その閉鎖から所定時間内は開放不能とされつつ開閉制御される
ことを特徴とする請求項1に記載の蒸気加熱装置。
The steam supply means includes a steam introduction pipe for supplying steam from a steam generator into the processing tank, and the steam supply operation valve including an electromagnetic valve provided in the middle of the steam introduction pipe,
The steam heating apparatus according to claim 1, wherein the steam supply operation valve is controlled to be opened and closed while the steam supply operation valve cannot be opened within a predetermined time from the closing thereof.
JP2006057948A 2006-03-03 2006-03-03 Steam heating apparatus Pending JP2007229379A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006057948A JP2007229379A (en) 2006-03-03 2006-03-03 Steam heating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006057948A JP2007229379A (en) 2006-03-03 2006-03-03 Steam heating apparatus

Publications (1)

Publication Number Publication Date
JP2007229379A true JP2007229379A (en) 2007-09-13

Family

ID=38550554

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006057948A Pending JP2007229379A (en) 2006-03-03 2006-03-03 Steam heating apparatus

Country Status (1)

Country Link
JP (1) JP2007229379A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010125998A1 (en) * 2009-04-27 2010-11-04 公立大学法人大阪市立大学 Vapor measurement device
JP2015169374A (en) * 2014-03-07 2015-09-28 株式会社サムソン Vacuum cooling apparatus
EP2605661B1 (en) * 2010-08-19 2018-01-24 BSH Hausgeräte GmbH Steam cooker
CN108618590A (en) * 2017-03-20 2018-10-09 佛山市顺德区美的电热电器制造有限公司 The control method of cooking apparatus and cooking apparatus
JP6457685B1 (en) * 2018-05-28 2019-01-23 株式会社マスダック Steamer and heat treatment method
EP3470739A1 (en) * 2017-10-12 2019-04-17 Miele & Cie. KG Cooking device and method for carrying out a processing process
JP2019213791A (en) * 2018-06-14 2019-12-19 株式会社吉田金属製作所 steamer
KR102072694B1 (en) * 2019-07-30 2020-02-03 주식회사 효신테크 A combi oven including the heat exchange module

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2010125998A1 (en) * 2009-04-27 2010-11-04 公立大学法人大阪市立大学 Vapor measurement device
JPWO2010125998A1 (en) * 2009-04-27 2012-11-01 公立大学法人大阪市立大学 Steam measuring device
EP2605661B1 (en) * 2010-08-19 2018-01-24 BSH Hausgeräte GmbH Steam cooker
JP2015169374A (en) * 2014-03-07 2015-09-28 株式会社サムソン Vacuum cooling apparatus
CN108618590A (en) * 2017-03-20 2018-10-09 佛山市顺德区美的电热电器制造有限公司 The control method of cooking apparatus and cooking apparatus
EP3470739A1 (en) * 2017-10-12 2019-04-17 Miele & Cie. KG Cooking device and method for carrying out a processing process
JP6457685B1 (en) * 2018-05-28 2019-01-23 株式会社マスダック Steamer and heat treatment method
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
JP2019213791A (en) * 2018-06-14 2019-12-19 株式会社吉田金属製作所 steamer
KR102072694B1 (en) * 2019-07-30 2020-02-03 주식회사 효신테크 A combi oven including the heat exchange module

Similar Documents

Publication Publication Date Title
JP2007229379A (en) Steam heating apparatus
JP2007222314A (en) Cooking apparatus and cooking method
JP5251557B2 (en) Cooling device and cooling method
JP4924147B2 (en) Food machine with vacuum cooling function and its operation method
JP4581846B2 (en) Steaming device
JP4055684B2 (en) Vacuum steam cooker
JP2006349287A (en) Vacuum cooling apparatus and method
JP4581849B2 (en) Steaming device
JP4867647B2 (en) Saturated steam heater
JP4428271B2 (en) Vacuum cooler, overcooling prevention device, and vacuum cooling method
JP5370670B2 (en) Operation method of cooking device
JP2007268018A (en) Steam-heating apparatus
JP4254521B2 (en) Cooking device operation control method and cooking device
JP2007187372A (en) Operation control method for cooker
JP4736126B2 (en) Steam cooking equipment
JP2018068528A (en) Steam sterilization device and operational method thereof
JP2007268017A (en) Steam-heating apparatus
JP2006181001A (en) Steaming/refrigerating system and steaming system
JP2007105452A (en) System and method for multiple processing tub control
JP2004218957A (en) Vacuum cooling method
JP4605542B2 (en) Steam cooking equipment
JP4640701B2 (en) Vacuum cooling device
JP4055676B2 (en) Steaming cooler
JP4605541B2 (en) Steam cooking equipment
JP2005046088A (en) Vacuum steam thawing machine