JP4581846B2 - Steaming device - Google Patents

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JP4581846B2
JP4581846B2 JP2005156047A JP2005156047A JP4581846B2 JP 4581846 B2 JP4581846 B2 JP 4581846B2 JP 2005156047 A JP2005156047 A JP 2005156047A JP 2005156047 A JP2005156047 A JP 2005156047A JP 4581846 B2 JP4581846 B2 JP 4581846B2
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pressure
steam
steaming
processing tank
treatment tank
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JP2006326090A (en
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暁 若狭
正敏 三浦
泰三 松川
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Miura Co Ltd
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Description

この発明は、蒸気を用いて食材を加熱調理する蒸煮装置に関するものである。 The present invention relates to cooking equipment for cooking the food using steam.

下記特許文献1に開示されるように、食材が入れられたメッシュ状のバスケットを蒸煮釜内に収容し、この蒸煮釜内へ蒸気を供給することで、食材を蒸し煮(蒸煮)して調理できる蒸煮装置が知られている。
特開平9−266856号公報
As disclosed in Patent Document 1 below, a mesh basket containing ingredients is stored in a steaming pot, and steam is supplied to the steaming pot to cook the ingredients (steamed). Steaming devices that can be used are known.
JP-A-9-266856

従来の蒸煮装置では、密閉され加圧または減圧された蒸煮釜内へ、継続的に蒸気を供給することで食材の加熱がなされていた。従って、このような加熱工程中、食材の撹拌を行うことはできなかった。食材の撹拌をなさずに加熱調理することは、食味の点から好ましくなかった。この発明が解決しようとする課題は、簡易な構成で、蒸煮中の食材の撹拌を可能とし、これにより食味の優れた煮物などを調理できる蒸煮装置を提供することにある。 In the conventional steaming apparatus, the food is heated by continuously supplying steam into the steaming pot that is sealed and pressurized or depressurized. Therefore, it was not possible to stir the food during such a heating process. It is not preferable from the point of taste to cook by heating without stirring the ingredients. Problems which the present invention is to provide a simple structure to allow stirring of the ingredients during cooking, thereby to provide a cooking equipment that can cook taste excellent boiled and the like.

この発明は、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、煮物用の具材と液体とからなる液物食材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、大気圧との差圧を利用して前記処理槽内から空気または蒸気を導出する排蒸手段と、前記処理槽内を減圧する減圧手段と、前記処理槽内の圧力を計測する圧力センサの出力に基づき前記各手段を制御する制御手段とを備え、前記処理槽内を大気圧より高圧として食材を蒸煮する加圧蒸煮と、前記処理槽内を大気圧より低圧として食材を蒸煮する減圧蒸煮との内、選択された蒸煮を実行可能とされ、前記処理槽内からの空気排除後、前記給蒸手段により前記処理槽内へ蒸気供給して、前記処理槽内を所望圧力P1に保持して食材を蒸煮中、前記処理槽内を設定圧力P2まで減圧後に前記所望圧力P1まで復圧する操作を、一回または複数回実行し、前記所望圧力P1および前記設定圧力P2は、変更可能とされ、前記設定圧力P2までの前記処理槽内の減圧は、加圧蒸煮中には前記排蒸手段と前記減圧手段との内、少なくとも前記排蒸手段を用いる一方、減圧蒸煮中には前記減圧手段を用いて行い、前記設定圧力P2から前記所望圧力P1までの復圧は、前記給蒸手段を用いて、前記処理槽内へ蒸気を供給して行い、前記設定圧力P2は、食材温度よりも低い飽和蒸気温度が得られる圧力で、且つ、減圧後の飽和蒸気温度と食材温度との温度差を設定範囲内とする圧力であることを特徴とする蒸煮装置である。 This invention was made in order to solve the said subject, The invention of Claim 1 is a processing tank in which the liquid foodstuff which consists of ingredients for boiled foods and a liquid is accommodated, In this processing tank Steam supply means for supplying steam to the steam, exhaust steam means for deriving air or steam from the treatment tank using a pressure difference from the atmospheric pressure, decompression means for reducing the pressure in the treatment tank, and in the treatment tank Control means for controlling the respective means based on the output of a pressure sensor for measuring the pressure of the pressure, steaming the food in the treatment tank at a pressure higher than the atmospheric pressure, and the treatment tank from the atmospheric pressure. Of the reduced-pressure steaming that steams the ingredients at low pressure, the selected steaming can be performed, and after the air is excluded from the processing tank, the steam is supplied into the processing tank by the steaming means, and the processing tank Inside the treatment tank while cooking the ingredients while keeping the inside at the desired pressure P1 The operation of returning to the desired pressure P1 after reducing the pressure to the set pressure P2 is performed once or a plurality of times, and the desired pressure P1 and the set pressure P2 can be changed, and the inside of the processing tank up to the set pressure P2 The depressurization of is performed using at least the exhausting means among the exhausting means and the decompressing means during the pressure steaming, while using the decompressing means during the steaming under reduced pressure. The return pressure to the desired pressure P1 is performed by supplying steam into the processing tank using the steaming means, and the set pressure P2 is a pressure at which a saturated steam temperature lower than the food material temperature is obtained, and The steaming apparatus is characterized in that the pressure is such that the temperature difference between the saturated steam temperature and the food material temperature after decompression is within a set range .

請求項1に記載の発明によれば、処理槽内へ蒸気を供給して食材を加熱中、処理槽内の圧力を一時的に下げることによって、食材の液体分を沸騰させ、それによって食材の撹拌を図ることができる。従って、煮物調理においても、煮汁の撹拌により、優れた食味に仕上げることができる。しかも、機械を用いて撹拌する訳ではないので、特別な装置が不要である。   According to the first aspect of the present invention, during the heating of the food by supplying steam into the processing tank, the pressure in the processing tank is temporarily lowered to boil the liquid content of the food, thereby Agitation can be achieved. Therefore, also in boiled food cooking, it can finish in the outstanding taste by stirring the soup. And since it is not necessarily stirred using a machine, a special apparatus is unnecessary.

この発明の蒸煮装置によれば、簡易な構成で、蒸煮中の食材の撹拌を可能とし、これにより食味の優れた煮物などを調理することができる。 According to the cooking equipment of the present invention, a simple configuration, to allow the agitation of the food during cooking, thereby it is possible to cook taste excellent boiled and the like.

つぎに、この発明の実施の形態について説明する。
本発明の蒸煮装置は、少なくとも一部に液状物を含んだ液物食材(食品を含む)の加熱調理に用いられ、特に、具材を煮汁と一緒に煮込む煮物類のように、固形分と液体分とからなる液物食材の加熱調理に好適に用いられる。
Next, an embodiment of the present invention will be described.
Cooking equipment of the present invention is used in cooking of containing liquid material to at least a portion the liquid product ingredients (including food), in particular, as boiled such that boil the ingredients together with broth, solids It is suitably used for cooking a liquid food material consisting of a liquid component.

本実施形態の蒸煮装置は、処理槽内に液物食材を収容した状態で、処理槽内へ蒸気を供給して、液物食材を加熱するものである。その際、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液物食材を加熱(加圧蒸煮)してもよいし、逆に、処理槽内の蒸気を吸引して外部へ排出したり、処理槽内の蒸気を凝縮させたりして、処理槽内を大気圧より低圧としつつ液物食材を加熱(減圧蒸煮)してもよい。 Cooking equipment of the present embodiment, in a state of accommodating the Ekibutsu foodstuff in the processing bath, and supplying steam to the process vessel, it is to heat the liquid product ingredients. At that time, the liquid food material may be heated (pressure steaming) while the inside of the processing tank is made higher than atmospheric pressure by the steam supplied into the processing tank, and conversely, the steam in the processing tank is sucked. The liquid food material may be heated (vacuum steamed) while discharging the outside or condensing the steam in the processing tank to make the inside of the processing tank at a pressure lower than the atmospheric pressure.

処理槽内への蒸気供給による液物食材の加熱工程中には、短時間だけ処理槽内の圧力を一時的に下げることで、液物食材内の液体分を沸騰させ、それにより液物食材の撹拌がなされる。この減圧は、一時的に処理槽内への蒸気供給を中止した状態で、処理槽外へ蒸気を吸引排出し、あるいはそれに代えてまたはそれに加えて、処理槽内の蒸気を凝縮させて行われる。また、加圧蒸煮の場合には、大気圧との差圧を利用して処理槽外へ蒸気を導出することによっても行うことができる。   During the heating process of the liquid food material by supplying steam into the processing tank, the liquid content in the liquid food material is boiled by temporarily lowering the pressure in the processing tank for a short time, thereby liquid food material Is agitated. This depressurization is performed by sucking and discharging the steam to the outside of the processing tank in a state where the supply of the steam to the processing tank is temporarily stopped, or condensing the steam in the processing tank instead of or in addition to that. . Moreover, in the case of pressure cooking, it can also carry out by guide | inducing vapor | steam outside a processing tank using differential pressure | voltage with atmospheric pressure.

液物食材を撹拌させるための処理槽内の一時的な減圧は、液物食材の液体分が沸騰する圧力までなされる。具体的には、液物食材の温度相当の飽和蒸気圧力以下にまで、処理槽内を減圧することで、液物食材を沸騰させることができる。つまり、食材温度よりも低い飽和蒸気温度が得られる圧力まで、処理槽内を減圧すればよい。   Temporary pressure reduction in the treatment tank for stirring the liquid food material is performed up to a pressure at which the liquid content of the liquid food material boils. Specifically, the liquid food material can be boiled by reducing the pressure in the treatment tank to a value equal to or lower than the saturated vapor pressure corresponding to the temperature of the liquid food material. That is, the inside of the treatment tank may be depressurized to a pressure at which a saturated steam temperature lower than the food material temperature is obtained.

ところで、従来は通常、煮物などの液物食材は、大気圧下において加熱調理される。大気圧下において開放状態の鍋で液物食材を加熱すると、やがて沸騰を生じるが、これは、100℃よりも高温の熱源によって加熱されるために、食材の一部または全部が飽和蒸気温度(100℃)またはそれを超える温度になるからである。ところが、蒸煮装置のように飽和蒸気環境下に食材をおいて加熱する場合、蒸気温度に比べて低温の食材に対し、周りの蒸気が凝縮することによって伝熱が行われる。そのため、通常、蒸煮装置内の食材は、常に飽和蒸気温度以下となり、沸騰がなされることはない。ところが、本発明の蒸煮装置においては、蒸煮中に、敢えて一時的に処理槽内を減圧することで、液物食材に沸騰を生じさせ、液物食材の撹拌が図られる。   By the way, conventionally, liquid food materials such as boiled food are cooked under atmospheric pressure. When a liquid food material is heated in an open pan under atmospheric pressure, it will eventually boil. This is heated by a heat source having a temperature higher than 100 ° C., so that part or all of the food material is saturated with a saturated steam temperature ( This is because the temperature becomes 100 ° C.) or higher. However, when a food is heated in a saturated steam environment like a steaming device, heat is transferred to the food having a temperature lower than the steam temperature by condensation of surrounding steam. Therefore, normally, the foodstuff in a steaming apparatus always becomes below a saturated steam temperature, and does not boil. However, in the steaming apparatus of the present invention, during the steaming, the processing tank is depressurized temporarily to cause boiling in the liquid food material, thereby stirring the liquid food material.

液物食材を撹拌させるための処理槽内の一時的な減圧は、どの程度の圧力または温度まで、どの程度の時間だけ行うかは適宜に設定される。この際、液物食材が沸騰を起こす程度の圧力または温度まで減圧することは必須である。また、減圧後の飽和蒸気温度と食材温度との温度差が大きい場合には、激しく沸騰して吹きこぼれが生じるおそれがあるので、前記温度差があまりに大きくならないよう設定される。そして、減圧下における保持時間としては、減圧後の飽和蒸気温度まで食材温度が下がって沸騰しなくなる程の時間を保持する必要はない。   It is set as appropriate as to how much time or how much pressure or temperature is temporarily reduced in the processing tank for stirring the liquid food material. At this time, it is essential to reduce the pressure to a pressure or temperature that causes the liquid food material to boil. In addition, when the temperature difference between the saturated steam temperature and the food material temperature after decompression is large, the temperature difference is set so that it does not become too large because there is a risk of violent boiling and spilling. As the holding time under reduced pressure, it is not necessary to hold such a time that the food material temperature falls to the saturated steam temperature after the pressure reduction and does not boil.

液物食材を撹拌させるための処理槽内の一時的な減圧は、処理槽内への蒸気供給による液物食材の加熱中、一または複数回なされる。このような蒸煮後には、処理槽内は大気圧まで復圧される。但し、処理槽内を減圧して液物食材を真空冷却してから、処理槽内を大気圧まで復圧するようにしてもよい。   Temporary pressure reduction in the processing tank for stirring the liquid food material is performed one or more times during heating of the liquid food material by supplying steam into the processing tank. After such steaming, the inside of the treatment tank is restored to atmospheric pressure. However, the inside of the processing tank may be decompressed to vacuum-cool the liquid food material, and then the inside of the processing tank may be returned to atmospheric pressure.

本実施形態の蒸煮装置は、処理槽に、給蒸手段、排蒸手段、減圧手段、復圧手段、および制御手段などが備えられて構成される。   The steaming apparatus of the present embodiment is configured such that a processing tank is provided with steaming means, steaming means, decompression means, decompression means, control means, and the like.

処理槽は、液物食材を収容して必要により密閉可能な容器である。処理槽には、加熱調理したい液物食材を入れた容器が収容される。この容器は、典型的には上方にのみ開口した容器とされ、その上部開口には吹きこぼれを防止するために、蒸気は通すが水は通さない性質を有した透湿防水性素材のシートで蓋をしてもよい。このような容器の処理槽内への収容は、処理槽内に設けた棚などに直接に置いてもよいし、処理槽に出し入れ可能なワゴンを介して行ってもよい。いずれの場合も、容器が載せられる棚はメッシュ状にされるなどして、蒸気が容器の全周囲に行き渡るようにするのがよい。   The treatment tank is a container that contains a liquid food material and can be sealed if necessary. The processing tank contains a container containing a liquid food material to be cooked. This container is typically a container that is opened only upward, and a top is covered with a sheet of moisture-permeable waterproof material that has the property of allowing steam to pass but not allowing water to pass through. You may do. Such accommodation of the container in the treatment tank may be directly placed on a shelf provided in the treatment tank or may be performed via a wagon that can be taken in and out of the treatment tank. In either case, the shelf on which the containers are placed may be meshed so that the vapor spreads all around the containers.

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。この際、衛生面を考慮して、一般的なボイラ(一次ボイラ)からの蒸気を利用して、別のボイラ(二次ボイラ)にて純水または軟水を蒸気変換し、この二次ボイラからの清浄蒸気を処理槽内へ供給するのがよい。   The steam supply means is means for supplying steam from the boiler into the treatment tank. At this time, in consideration of hygiene, steam from a general boiler (primary boiler) is converted into steam from pure water or soft water in another boiler (secondary boiler). It is preferable to supply the clean steam into the treatment tank.

排蒸手段は、処理槽の空気や蒸気を、処理槽内から外部へ導出する手段である。典型的には、処理槽の内外を連通する配管からなる排蒸ラインと、この排蒸ラインの中途に設けられて前記連通の有無やその度合いを調整する排蒸弁とからなる。従って、特に給蒸手段による蒸気供給により処理槽内が加圧された状態では、排蒸手段による処理槽外への蒸気の排出は、前記排蒸弁を開けるだけで、処理槽内圧力と大気圧との差圧を利用して自然に行うことができる。   The steaming means is a means for deriving the air and steam of the processing tank from the inside of the processing tank to the outside. Typically, it comprises a steaming line composed of piping that communicates the inside and outside of the treatment tank, and a steaming valve that is provided in the middle of this steaming line and adjusts the presence or absence of the communication. Therefore, particularly in a state where the inside of the treatment tank is pressurized by the steam supply by the steam supply means, the discharge of the steam to the outside of the treatment tank by the exhaust steam means can be performed by simply opening the exhaust steam valve and the pressure inside the treatment tank. It can be performed naturally using the pressure difference from the atmospheric pressure.

減圧手段は、処理槽内の空気や蒸気を外部へ吸引排気し、あるいは処理槽内の蒸気を凝縮させることで、処理槽内を減圧する手段である。この減圧手段は、典型的には、処理槽内を減圧する真空ポンプおよび/またはエゼクタを備えて構成される。また、真空ポンプを用いる場合には、真空ポンプの手前に熱交換器を備えておくことで、蒸気を凝縮させて減圧能力を高めることができる。この減圧手段は、その減圧能力が調整可能なものが好ましい。   The decompression means is means for decompressing the inside of the processing tank by sucking and exhausting air or steam in the processing tank to the outside or condensing the steam in the processing tank. The decompression means typically includes a vacuum pump and / or an ejector that decompresses the inside of the processing tank. Moreover, when using a vacuum pump, by providing a heat exchanger in front of the vacuum pump, it is possible to condense the vapor and increase the pressure reduction capability. The decompression means is preferably one that can adjust its 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。   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.

制御手段は、前記給蒸手段、前記排蒸手段、前記減圧手段、および前記復圧手段を制御して、処理槽内の液物食材を加熱し、その後、所望により真空冷却する手段である。液物食材の調理のためには、典型的には予熱および空気排除工程の後、蒸煮工程(加熱工程)がなされる。これら制御は、処理槽内の圧力を計測する圧力センサを利用してなされる。但し、処理槽内の圧力は、温度と所定の関係を有するので、圧力センサに代えて温度センサを用いることも可能である。また、本実施形態では、処理槽内に収容した液物食材の温度を計測する温度センサも利用して制御がなされる。さらに、前記各手段を作動させる時間を調整して、処理槽内を所望の圧力または温度に調整することもできる。   The control means is means for controlling the steam supply means, the steaming means, the pressure reducing means, and the pressure-reducing means to heat the liquid food material in the processing tank, and then vacuum-cooling it as desired. For cooking a liquid food material, typically, after a preheating and air exclusion process, a steaming process (heating process) is performed. These controls are performed using a pressure sensor that measures the pressure in the treatment tank. However, since the pressure in the treatment tank has a predetermined relationship with the temperature, it is possible to use a temperature sensor instead of the pressure sensor. In the present embodiment, control is also performed using a temperature sensor that measures the temperature of the liquid food contained in the processing tank. Furthermore, it is also possible to adjust the time for operating each of the means to adjust the inside of the processing tank to a desired pressure or temperature.

予熱および空気排除工程は、給蒸手段により処理槽内へ蒸気供給して、処理槽内の空気を処理槽外へ排蒸手段を介して排出すると共に、液物食材を予熱する工程である。また、減圧手段による減圧後に給蒸手段による蒸気供給や、給蒸手段による蒸気供給後に排蒸手段による空気排除を、それぞれ所望回数行ってもよい。   The preheating and air exclusion step is a step of supplying steam into the processing tank by the steam supply means, discharging the air in the processing tank to the outside of the processing tank through the steaming means, and preheating the liquid food material. Further, the steam supply by the steam supply means after the decompression by the decompression means and the air removal by the steaming means after the steam supply by the steam supply means may be performed as many times as desired.

蒸煮工程は、空気排除された処理槽内へ給蒸手段により蒸気供給して、食材を加熱する工程である。この際、前述したように、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液物食材を加圧蒸煮してもよいし、逆に、減圧手段により処理槽内を大気圧より低圧としつつ液物食材を減圧蒸煮してもよい。そして、本発明においては、この蒸煮工程中に、液物食材の撹拌処理が一または複数回行われる。   The steaming step is a step of heating the food by supplying steam into the processing tank from which air has been removed by steaming means. At this time, as described above, the liquid food material may be steamed under pressure while the inside of the processing tank is set to a pressure higher than the atmospheric pressure by the steam supplied into the processing tank. The liquid food material may be steamed under reduced pressure while the pressure is lower than atmospheric pressure. And in this invention, the stirring process of a liquid foodstuff is performed 1 or more times during this cooking process.

この撹拌処理は、一時的に処理槽内への蒸気供給を中止した状態で、処理槽内を短時間だけ減圧して、液物食材内の液体分を沸騰させることで、液物食材の撹拌を行うものである。減圧蒸煮の場合には、減圧手段により処理槽内の蒸気を外部へ真空引きして減圧することにより短時間の減圧を行うことができる。また、加圧蒸煮の場合には、排蒸手段により処理槽内の圧力を開放することにより短時間の減圧を行うことができ、さらに所望により、減圧手段による減圧を併用してもよい。撹拌処理には、再び処理槽内へ蒸気供給を行い、液物食材の蒸煮がなされる。 In this stirring process, the supply of steam into the processing tank is temporarily stopped, the pressure in the processing tank is reduced for a short time, and the liquid content in the liquid food is boiled, thereby stirring the liquid food. Is to do. In the case of reduced-pressure steaming, a short-time pressure reduction can be performed by evacuating the steam in the treatment tank to the outside by the pressure reducing means. Further, in the case of pressure steaming, the pressure in the treatment tank can be released by releasing the pressure in the treatment tank, and the pressure reduction by the pressure reduction means may be used together if desired. After stirring treatment performs steam supply again to the processing bath, steaming is made of a liquid product ingredients.

このような撹拌処理を伴う蒸煮工程の終了後には、処理槽内を大気圧まで復圧して、一連の処理を完了する。但し、所望により、減圧手段により処理槽内を減圧保持して、液物食材の冷却を図る真空冷却工程を行ってもよい。   After the completion of the steaming process involving such a stirring process, the inside of the treatment tank is restored to atmospheric pressure, and a series of processes is completed. However, if desired, a vacuum cooling process may be performed in which the inside of the treatment tank is held under reduced pressure by a decompression unit to cool the liquid food material.

以下、この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、本発明の蒸煮装置の一実施例を示す概略構造図である。この図に示すように、本実施例の蒸煮装置は、上方にのみ開口した容器1に入れられた液物食材2を収容する処理槽3と、処理槽3内へ蒸気を供給する給蒸手段4と、処理槽3内から空気や蒸気を外部へ導出する排蒸手段5と、処理槽3内を真空引きして減圧する減圧手段6と、減圧下の処理槽3内へ外気を導入して復圧する復圧手段7と、処理槽3内の圧力を計測する圧力センサ8と、処理槽3内の食材温度を計測する温度センサ9とを主要部として備える。温度センサ9は、食材温度を非接触で検出するものでもよいが、図示例では液物食材2に差し込まれて食材温度を検出するものである。
Hereinafter, specific embodiments of the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic structural diagram showing an embodiment of the steaming apparatus of the present invention. As shown in this figure, the steaming apparatus of the present embodiment includes a processing tank 3 for storing a liquid food material 2 placed in a container 1 opened only upward, and steaming means for supplying steam into the processing tank 3. 4, a steaming means 5 for deriving air and steam from the inside of the treatment tank 3, a decompression means 6 for evacuating and decompressing the inside of the treatment tank 3, and introducing outside air into the treatment tank 3 under reduced pressure The pressure recovery means 7 for returning pressure, the pressure sensor 8 for measuring the pressure in the processing tank 3, and the temperature sensor 9 for measuring the temperature of the food in the processing tank 3 are provided as main parts. The temperature sensor 9 may detect the food temperature without contact, but in the illustrated example, the temperature sensor 9 is inserted into the liquid food 2 to detect the food temperature.

本実施例の処理槽3は、中空ボックス状の処理槽本体10にドア11が開閉可能に設けられており、耐圧性を有する構造とされている。ドアは11、開き戸、引き戸、または上下方向に可動するシャッター式のいずれでもよい。ところで、前記容器1に入れられた液物食材2の処理槽3への出し入れは、本実施例ではワゴン12を介してなされる。ワゴン12は、底部にキャスター13,13…を有する。   The processing tank 3 of the present embodiment is provided with a door 11 in a hollow box-shaped processing tank main body 10 so that it can be opened and closed, and has a pressure resistant structure. The door may be any of 11, a hinged door, a sliding door, or a shutter type movable in the vertical direction. By the way, the liquid food material 2 put in the container 1 is put into and out of the treatment tank 3 through the wagon 12 in this embodiment. The wagon 12 has casters 13, 13... At the bottom.

給蒸手段4は、処理槽3内へ蒸気を供給(給蒸)する手段である。本実施例の給蒸手段4は、一次ボイラ(不図示)と二次ボイラ(リボイラ)14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14にて軟水を蒸気に変え、このようにして生成された清浄蒸気を処理槽3内へ供給する。   The steam supply means 4 is means for supplying (steaming) steam into the treatment tank 3. The steam supply means 4 of the present embodiment includes a primary boiler (not shown) and a secondary boiler (reboiler) 14. Using the steam from the primary boiler as a heat source, the soft water is changed to steam by the secondary boiler 14. The clean steam thus generated is supplied into the treatment tank 3.

具体的には、二次ボイラ14は、ステンレス製の熱交換器15であり、給水管16からの軟水を加熱して蒸気に変換する。軟水を加熱するために、二次ボイラ14には、給蒸管17を介して一次ボイラからの蒸気が供給される。このようにして一次ボイラから供給された蒸気は、二次ボイラ14のステンレス配管内へ供給される軟水を加熱する。これにより、二次ボイラ14にて、軟水により清浄蒸気が生成される。   Specifically, the secondary boiler 14 is a stainless steel heat exchanger 15 that heats soft water from the water supply pipe 16 and converts it into steam. In order to heat the soft water, steam from the primary boiler is supplied to the secondary boiler 14 via the steam supply pipe 17. Thus, the steam supplied from the primary boiler heats the soft water supplied into the stainless steel pipe of the secondary boiler 14. Thereby, clean steam is generated by the soft water in the secondary boiler 14.

二次ボイラ14にて生成された清浄蒸気は、蒸気供給用配管としての給蒸ライン18を介して、処理槽3内へ供給される。給蒸ライン18の中途には、処理槽給蒸弁19が設けられている。この処理槽給蒸弁19は、処理槽3内への給蒸の有無と、給蒸する場合の蒸気量を調整可能な構成であり、典型的には比例制御弁から構成される。この処理槽給蒸弁19を調整することで、処理槽3内の圧力、ひいては温度を調整することができる。但し、処理槽内3の圧力調整は、処理槽給蒸弁19だけでなく減圧手段6を制御することによっても、行うことができる。   The clean steam generated in the secondary boiler 14 is supplied into the processing tank 3 via a steam supply line 18 as a steam supply pipe. In the middle of the steam supply line 18, a treatment tank steam supply valve 19 is provided. The processing tank steam supply valve 19 is configured to be capable of adjusting the presence / absence of steaming into the processing tank 3 and the amount of steam when steaming, and is typically composed of a proportional control valve. By adjusting the processing tank steam supply valve 19, the pressure in the processing tank 3 and thus the temperature can be adjusted. However, the pressure adjustment in the processing tank 3 can be performed by controlling not only the processing tank steam supply valve 19 but also the decompression means 6.

排蒸手段5は、処理槽3内から空気または蒸気を外部へ導出する手段である。具体的には、蒸気排出用配管としての排蒸ライン20からなり、この排蒸ライン20を介して処理槽3内の空気や蒸気が処理槽3外へ導出される。本実施例では、処理槽3の上部から、第一排蒸弁21と逆止弁22を介して蒸気などが排出可能とされる一方、処理槽3の下部からも第二排蒸弁23を介して排出可能とされている。これら各排蒸弁21,23は、比例制御弁などの開度調整可能な弁から構成するのがよく、この開度を調整することで、処理槽3の内外の連通度合いが調整される。   The steaming means 5 is a means for deriving air or steam from the processing tank 3 to the outside. Specifically, it consists of a steaming line 20 as a steam discharge pipe, and air and steam in the processing tank 3 are led out of the processing tank 3 through this steaming line 20. In this embodiment, steam or the like can be discharged from the upper part of the processing tank 3 via the first exhaust valve 21 and the check valve 22, while the second exhaust valve 23 is also connected from the lower part of the processing tank 3. It can be discharged through. Each of these exhaust steam valves 21 and 23 is preferably composed of a valve whose opening degree can be adjusted, such as a proportional control valve, and the degree of communication inside and outside the treatment tank 3 is adjusted by adjusting the opening degree.

減圧手段6は、本実施例では、蒸気エゼクタ24と熱交換器25と真空ポンプ26とを組み合わせて構成される。この場合、蒸気エゼクタ24は、処理槽3に吸入口27が接続されており、この蒸気エゼクタ24の出口28には、熱交換器25と逆止弁29を介して真空ポンプ26が接続される。従って、真空ポンプ26を作動させつつ、蒸気エゼクタ24の入口30から出口28へ向けて蒸気を噴射させることで、吸入口27が接続された処理槽3内の空気を吸引排出し、処理槽3内を減圧することができる。この際、真空ポンプ26の手前に熱交換器25を設けることで、蒸気を冷却および凝縮させることができ、効率的な減圧が可能とされる。   In this embodiment, the decompression means 6 is configured by combining a steam ejector 24, a heat exchanger 25, and a vacuum pump 26. In this case, the steam ejector 24 has a suction port 27 connected to the processing tank 3, and a vacuum pump 26 is connected to the outlet 28 of the steam ejector 24 via a heat exchanger 25 and a check valve 29. . Therefore, by operating the vacuum pump 26 and injecting steam from the inlet 30 to the outlet 28 of the steam ejector 24, the air in the processing tank 3 to which the suction port 27 is connected is sucked and discharged. The inside can be depressurized. At this time, by providing the heat exchanger 25 in front of the vacuum pump 26, the steam can be cooled and condensed, and efficient decompression can be performed.

このようなことを達成するために、蒸気エゼクタ24の入口30には、エゼクタ給蒸弁31を介して、前記二次ボイラ14からの蒸気が供給可能とされる。つまり、本実施例では、二次ボイラ14からの蒸気は、蒸気エゼクタ24の入口30への給蒸と、処理槽3内への給蒸の双方に利用される。この切換えは、エゼクタ給蒸弁31や処理槽給蒸弁19の開閉にて行うことができる。但し、一次ボイラ(不図示)だけを用いて、そのボイラの蒸気をエゼクタ24や処理槽3への供給に利用可能である。また、処理槽3へは二次ボイラ14からの清浄蒸気を供給し、エゼクタ24へは一次ボイラからの蒸気を供給するようにしてもよい。   In order to achieve this, the steam from the secondary boiler 14 can be supplied to the inlet 30 of the steam ejector 24 via the ejector steam supply valve 31. That is, in the present embodiment, the steam from the secondary boiler 14 is used for both steam supply to the inlet 30 of the steam ejector 24 and steam supply to the treatment tank 3. This switching can be performed by opening and closing the ejector steam supply valve 31 and the processing tank steam supply valve 19. However, only the primary boiler (not shown) can be used to supply the steam of the boiler to the ejector 24 and the processing tank 3. Further, clean steam from the secondary boiler 14 may be supplied to the treatment tank 3, and steam from the primary boiler may be supplied to the ejector 24.

また、上述したように、蒸気エゼクタ24の出口28には、熱交換器25と逆止弁29を介して、水封式真空ポンプ26が接続される。この真空ポンプ26には、封水給水弁32を介して水が供給され、真空ポンプ26からの排水は、排水口(不図示)へ排出される。また、熱交換器25にも、熱交給水弁33を介して冷却用の水が供給され、排水口へ排水される。真空ポンプ26へ給水用の封水給水弁32は、真空ポンプ26に連動して開かれる。   Further, as described above, the water-sealed vacuum pump 26 is connected to the outlet 28 of the steam ejector 24 via the heat exchanger 25 and the check valve 29. Water is supplied to the vacuum pump 26 through a sealed water supply valve 32, and the waste water from the vacuum pump 26 is discharged to a drain port (not shown). In addition, cooling water is also supplied to the heat exchanger 25 through the heat exchange water supply valve 33 and drained to the drain outlet. A sealed water supply valve 32 for supplying water to the vacuum pump 26 is opened in conjunction with the vacuum pump 26.

ところで、減圧手段は、その減圧能力が調整可能なものが好ましい。そのためには、エゼクタ給蒸弁31の開度を調整して、蒸気エゼクタ24の能力を制御すればよい。あるいは、インバータを用いて、真空ポンプ26の回転数を制御してもよい。また、熱交給水弁33の開度を調整して、熱交換器25への給水量を調整したり、その給水温度を調整したりしてもよい。   By the way, it is preferable that the decompression means can adjust its decompression capability. For that purpose, the opening degree of the ejector steam supply valve 31 may be adjusted to control the capability of the steam ejector 24. Or you may control the rotation speed of the vacuum pump 26 using an inverter. Moreover, the opening degree of the heat exchange water supply valve 33 may be adjusted to adjust the amount of water supplied to the heat exchanger 25, or the water supply temperature thereof may be adjusted.

復圧手段7は、処理槽3内の真空状態を解除可能に、処理槽3内へ外気を導入する手段である。本実施例では、処理槽3は、外気導入弁34とフィルター35とを介して、外気に連通可能とされている。従って、外気導入弁34を開くと、処理槽3内は大気圧下に開放され、フィルター35を介して処理槽3内へ外気を導入して、処理槽3内を復圧可能である。外気導入弁34の開き具合によって、処理槽3内を徐々に昇圧することもできる。   The return pressure means 7 is a means for introducing outside air into the processing tank 3 so that the vacuum state in the processing tank 3 can be released. In this embodiment, the processing tank 3 can communicate with the outside air via the outside air introduction valve 34 and the filter 35. Therefore, when the outside air introduction valve 34 is opened, the inside of the processing tank 3 is opened to the atmospheric pressure, and outside air can be introduced into the processing tank 3 through the filter 35 and the inside of the processing tank 3 can be restored. Depending on how the outside air introduction valve 34 is opened, the pressure in the processing tank 3 can be gradually increased.

また、蒸煮装置には、給蒸手段4、排蒸手段5、減圧手段6、復圧手段7などを制御する制御手段36が備えられている。この制御手段36は、それが把握する時間の他、処理槽内圧力を検出する圧力センサ8や、食材温度を検出する温度センサ9からの検出信号などに基づいて、前記各手段4〜7を制御する制御器である。具体的には、処理槽給蒸弁19、各排蒸弁21,23、真空ポンプ26、エゼクタ給蒸弁31、封水給水弁32、熱交給水弁33、外気導入弁34、圧力センサ8および温度センサ9は、制御器36に接続されている。そして、この制御器36は、所定の手順(プログラム)に基づき、後述するように、処理槽3内の液物食材2の蒸煮を行う。   Further, the steaming device is provided with a control means 36 for controlling the steam supply means 4, the exhaust steam means 5, the decompression means 6, the decompression means 7, and the like. The control means 36 controls the means 4 to 7 based on a detection signal from the pressure sensor 8 for detecting the pressure in the processing tank and the temperature sensor 9 for detecting the food temperature, in addition to the time to be grasped. It is a controller to control. Specifically, the treatment tank steam supply valve 19, the exhaust steam valves 21 and 23, the vacuum pump 26, the ejector steam supply valve 31, the sealed water supply valve 32, the heat exchange water supply valve 33, the outside air introduction valve 34, and the pressure sensor 8. The temperature sensor 9 is connected to the controller 36. And this controller 36 steams the liquid foodstuff 2 in the processing tank 3 so that it may mention later based on a predetermined | prescribed procedure (program).

図2は、本実施例の蒸煮装置の運転中における処理槽3内の圧力変化の一例を示す図である。本実施例の蒸煮装置は、具材と煮汁とからなる煮物類などの加熱調理に好適に用いられる。具体的には、上方へ開口した金属製容器1内に、具材となる固形分と、煮汁となる液体分とを一緒に入れた後、その容器1を処理槽3内へ収容して、煮物を調理する。そのために、通常、予熱および空気排除工程の後、蒸煮工程を行う。   FIG. 2 is a diagram illustrating an example of a pressure change in the treatment tank 3 during the operation of the steaming apparatus according to the present embodiment. The steaming apparatus of a present Example is used suitably for heat cooking, such as simmered goods which consist of ingredients and soup. Specifically, in the metal container 1 opened upward, after putting together the solid content to be ingredients and the liquid content to be boiled juice, the container 1 is accommodated in the treatment tank 3, Cook boiled food. For this purpose, a steaming step is usually performed after the preheating and air exclusion step.

予熱および空気排除工程では、各排蒸弁21,23のみを開いた状態で、さらに処理槽給蒸弁19も開いて、処理槽3内へ蒸気を供給し、所定時間経過後に処理槽給蒸弁19を閉じて、処理槽3内の空気を排蒸ライン20を介して処理槽3外へ排出する。この際、予め処理槽3内を減圧手段6により減圧してから、その減圧下の処理槽3内へ給蒸手段4によって、蒸気を供給するようにしてもよい。   In the preheating and air exclusion process, only the exhaust steam valves 21 and 23 are opened, the processing tank steam supply valve 19 is also opened, steam is supplied into the processing tank 3, and the processing tank steaming is performed after a predetermined time has elapsed. The valve 19 is closed, and the air in the processing tank 3 is discharged out of the processing tank 3 via the exhaust line 20. At this time, the inside of the treatment tank 3 may be decompressed by the decompression means 6 in advance, and then the steam may be supplied by the steam supply means 4 into the treatment tank 3 under the decompression.

本実施例の蒸煮工程は、給蒸手段4による処理槽3内への蒸気供給と、それによる処理槽3内の加圧を伴うものである。言い換えれば、処理槽3内を大気圧よりも高圧にするように、処理槽3内へ蒸気を供給して、液物食材2を加圧蒸煮する。具体的には、エゼクタ給蒸弁31、外気導入弁34、および各排蒸弁21,23を閉じた状態で、処理槽給蒸弁19を開いて、処理槽3内へ蒸気を供給する。この際、上述したように、処理槽3内へ供給される蒸気は、二次ボイラ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、容器1の全周囲に清浄蒸気を行き渡らせることで、短時間で均一な加熱調理がなされる。   The steaming process of the present embodiment involves supplying steam into the processing tank 3 by the steam supply means 4 and pressurizing the processing tank 3 thereby. In other words, steam is supplied into the processing tank 3 so that the inside of the processing tank 3 has a pressure higher than the atmospheric pressure, and the liquid food material 2 is steamed under pressure. Specifically, with the ejector steam supply valve 31, the outside air introduction valve 34, and the exhaust steam valves 21 and 23 being closed, the processing tank steaming valve 19 is opened to supply steam into the processing tank 3. At this time, as described above, the steam supplied into the treatment tank 3 is clean steam generated from soft water in the secondary boiler 14. Therefore, safe and reliable cooking can be realized. Moreover, uniform cooking is performed in a short time by spreading clean steam around the entire periphery of the container 1.

蒸煮工程では、処理槽給蒸弁19の開度を調整して、処理槽3内への蒸気供給量を調整することにより、処理槽3内の圧力ひいては温度が調整される。具体的には、制御器36は、圧力センサ8の出力に基づき、処理槽給蒸弁19の開度を調整する。このようにして処理槽3内の圧力を調整することで、処理槽3内の飽和蒸気温度が調整される。本実施例では図2に示すように、所望圧力P1まで処理槽3内を昇圧した後、その所望圧力P1にて所望時間だけ保持される。   In the steaming step, the pressure in the processing tank 3 and the temperature are adjusted by adjusting the opening of the processing tank supply valve 19 and adjusting the amount of steam supplied into the processing tank 3. Specifically, the controller 36 adjusts the opening degree of the treatment tank steam supply valve 19 based on the output of the pressure sensor 8. By adjusting the pressure in the processing tank 3 in this way, the saturated steam temperature in the processing tank 3 is adjusted. In this embodiment, as shown in FIG. 2, after the pressure in the processing tank 3 is increased to the desired pressure P1, the pressure is maintained at the desired pressure P1 for a desired time.

本実施例では、この所望圧力P1を大気圧より高くすることで、液物食材2を加圧蒸煮しているが、大気圧より低く設定することで、液物食材2を減圧蒸煮することもできる。この場合、減圧手段6を作動させて処理槽3内を減圧しつつ、給蒸手段4により処理槽3内へ蒸気供給すればよい。   In the present embodiment, the liquid food material 2 is steamed under pressure by making the desired pressure P1 higher than the atmospheric pressure, but the liquid food material 2 may be steamed under reduced pressure by setting it lower than the atmospheric pressure. it can. In this case, steam may be supplied into the treatment tank 3 by the steam supply means 4 while the decompression means 6 is operated to decompress the inside of the treatment tank 3.

蒸煮工程中には、図2に示すように処理槽3内を一時的に設定圧力P2まで減圧して、液物食材2を沸騰させることで液物食材2の撹拌を図る撹拌処理が少なくとも一回は行われる。この撹拌処理中には、処理槽給蒸弁19が一時的に閉められ、処理槽3内への蒸気供給が一時的に中止される。そして、その状態で処理槽3内を設定圧力まで短時間だけ減圧される。加圧蒸煮中の減圧は、各排蒸弁21,23を開いて、処理槽3内の圧力を開放すればよい。また、減圧蒸煮中には、減圧手段6を作動させて処理槽3内を減圧すればよい。具体的には、エゼクタ給蒸弁31や封水給水弁32および熱交給水弁33を開いた状態で、真空ポンプ26を作動させればよい。   During the steaming process, as shown in FIG. 2, at least one stirring process is performed in which the liquid food material 2 is stirred by temporarily reducing the pressure in the processing tank 3 to the set pressure P <b> 2 and boiling the liquid food material 2. Times are done. During the stirring process, the treatment tank steam supply valve 19 is temporarily closed, and the supply of steam into the treatment tank 3 is temporarily stopped. In this state, the inside of the processing tank 3 is reduced to a set pressure for a short time. The decompression during the pressure cooking may be performed by opening the exhaust steam valves 21 and 23 to release the pressure in the treatment tank 3. Moreover, what is necessary is just to depressurize the inside of the processing tank 3 by operating the pressure-reduction means 6 during vacuum cooking. Specifically, the vacuum pump 26 may be operated with the ejector feed valve 31, the sealed water feed valve 32, and the heat exchange feed valve 33 open.

撹拌処理のための処理槽3内の減圧は、食材温度よりも低い飽和蒸気温度が得られる圧力までなされる。そのために、本実施例では、まず温度センサ9により食材温度が検出され、この食材温度相当の飽和蒸気圧力以下にまで減圧される。これにより、処理槽3内の液物食材2の液体分(煮汁)を沸騰させ、これにより液物食材2全体を撹拌することができる。たとえば、120℃蒸煮中に100℃相当の圧力まで減圧するが、これら温度は適宜変更可能なことは言うまでもない。   The pressure in the treatment tank 3 for the stirring treatment is reduced to a pressure at which a saturated steam temperature lower than the food material temperature is obtained. Therefore, in this embodiment, first, the food temperature is detected by the temperature sensor 9, and the pressure is reduced to below the saturated vapor pressure corresponding to the food temperature. Thereby, the liquid part (boiled juice) of the liquid foodstuff 2 in the processing tank 3 can be boiled, and, thereby, the liquid foodstuff 2 whole can be stirred. For example, the pressure is reduced to a pressure corresponding to 100 ° C. during cooking at 120 ° C., but it goes without saying that these temperatures can be changed as appropriate.

このように、本実施例によれば、撹拌装置のような特別の装置を用いることなく、蒸煮中の食材2を撹拌することができる。ところで、液物食材2が入れられた容器1内へ外部から空気を導入して撹拌を図ってもよい。この場合、容器1内への空気の導入は、ポンプなどを用いて強制的に吹き込んでもよいが、処理槽3内が減圧下にある場合には、処理槽3の内外の圧力差に基づき、自然に空気を送り込むことが可能である。   Thus, according to the present Example, the foodstuff 2 in cooking can be stirred, without using a special apparatus like a stirring apparatus. By the way, air may be introduced from the outside into the container 1 in which the liquid food material 2 is placed to stir. In this case, the introduction of air into the container 1 may be forcibly blown using a pump or the like, but when the inside of the processing tank 3 is under reduced pressure, based on the pressure difference between the inside and outside of the processing tank 3, It is possible to send air naturally.

この場合、中途部に開閉弁(不図示)を設けた管路からなる空気導入ライン(不図示)を、処理槽の3内外を連通するように設ければよい。そして、この空気導入ラインは、一端部がフィルター(不図示)を介して大気圧下に開放されており、他端部は前記容器1内に開放される。これにより、前記減圧手段6による前記処理槽3内の減圧下で、前記開閉弁を開くことにより、処理槽3の内外の圧力差により、フィルターを介した空気が容器1内に導入される。空気導入ラインを介した前記容器1内への空気導入は、前記容器1の底部から行うのがよい。これにより、液物食材2内に気泡が上昇することで、液物食材2を撹拌することができる。但し、空気を入れた場合の伝熱障害などを考慮すれば、空気を導入せずに処理槽3内を減圧するだけで撹拌するのが望ましい。   In this case, an air introduction line (not shown) composed of a pipe line provided with an on-off valve (not shown) in the middle may be provided so as to communicate between the inside and outside of the treatment tank 3. One end of the air introduction line is opened under atmospheric pressure via a filter (not shown), and the other end is opened in the container 1. Thereby, air through the filter is introduced into the container 1 due to the pressure difference between the inside and outside of the processing tank 3 by opening the on-off valve under the reduced pressure in the processing tank 3 by the pressure reducing means 6. The introduction of air into the container 1 through the air introduction line is preferably performed from the bottom of the container 1. Thereby, the liquid foodstuff 2 can be stirred because the bubble rises in the liquid foodstuff 2. However, in consideration of heat transfer failure when air is introduced, it is desirable to stir only by reducing the pressure in the treatment tank 3 without introducing air.

このような撹拌処理を伴う蒸煮工程の終了後には、処理槽給蒸弁19を閉じて、処理槽3内を大気圧まで復圧して全工程を終了する。この復圧は、加圧蒸煮の場合には、各排蒸弁21,23を開けばよいし、減圧蒸煮の場合には、外気導入弁34を開けばよい。   After the completion of the steaming process involving such a stirring process, the processing tank steam supply valve 19 is closed, the pressure in the processing tank 3 is restored to atmospheric pressure, and all the processes are completed. In the case of pressure steaming, this return pressure can be achieved by opening the exhaust steam valves 21 and 23, and in the case of vacuum steaming, the outside air introduction valve 34 can be opened.

本発明の蒸煮装置は、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、蒸煮工程中における撹拌処理は、加圧蒸煮の場合には、排蒸手段5による処理槽3内の圧力開放だけでなく、所望により減圧手段6による処理槽3内の減圧をも併用することができる。また、処理槽3内の減圧速度を遅くすることで、吹きこぼれを防止することができる。 Cooking equipment of the present invention may be appropriately modified without limited to the configuration of the embodiment. For example, in the case of pressure steaming, the stirring process during the steaming process uses not only the pressure release in the processing tank 3 by the steaming means 5 but also the pressure reduction in the processing tank 3 by the pressure reducing means 6 if desired. be able to. Moreover, it is possible to prevent spillage by slowing down the pressure reduction rate in the treatment tank 3.

本発明の蒸煮装置の一実施例を示す概略構造図である。It is a schematic structure figure showing one example of the steaming device of the present invention. 図1の蒸煮装置の運転中における処理槽内の圧力変化の一例を示す図である。It is a figure which shows an example of the pressure change in a processing tank in the driving | operation of the cooking apparatus of FIG.

符号の説明Explanation of symbols

1 容器
2 液物食材
3 処理槽
4 給蒸手段
5 排蒸手段
6 減圧手段
7 復圧手段
8 圧力センサ
9 温度センサ
36 制御手段(制御器)
DESCRIPTION OF SYMBOLS 1 Container 2 Liquid food material 3 Processing tank 4 Steaming means 5 Dehumidifying means 6 Depressurizing means 7 Restoring means 8 Pressure sensor 9 Temperature sensor 36 Control means (controller)

Claims (1)

煮物用の具材と液体とからなる液物食材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、
大気圧との差圧を利用して前記処理槽内から空気または蒸気を導出する排蒸手段と、
前記処理槽内を減圧する減圧手段と、
前記処理槽内の圧力を計測する圧力センサの出力に基づき前記各手段を制御する制御手段とを備え、
前記処理槽内を大気圧より高圧として食材を蒸煮する加圧蒸煮と、前記処理槽内を大気圧より低圧として食材を蒸煮する減圧蒸煮との内、選択された蒸煮を実行可能とされ、
前記処理槽内からの空気排除後、前記給蒸手段により前記処理槽内へ蒸気供給して、前記処理槽内を所望圧力P1に保持して食材を蒸煮中、前記処理槽内を設定圧力P2まで減圧後に前記所望圧力P1まで復圧する操作を、一回または複数回実行し、
前記所望圧力P1および前記設定圧力P2は、変更可能とされ、
前記設定圧力P2までの前記処理槽内の減圧は、加圧蒸煮中には前記排蒸手段と前記減圧手段との内、少なくとも前記排蒸手段を用いる一方、減圧蒸煮中には前記減圧手段を用いて行い、
前記設定圧力P2から前記所望圧力P1までの復圧は、前記給蒸手段を用いて、前記処理槽内へ蒸気を供給して行い、
前記設定圧力P2は、食材温度よりも低い飽和蒸気温度が得られる圧力で、且つ、減圧後の飽和蒸気温度と食材温度との温度差を設定範囲内とする圧力である
ことを特徴とする蒸煮装置。
A processing tank in which liquid ingredients composed of ingredients for boiled food and liquid are stored ;
Steam supply means for supplying steam into the treatment tank;
A steaming means for deriving air or steam from the inside of the treatment tank using a pressure difference from the atmospheric pressure;
Decompression means for decompressing the inside of the treatment tank;
Control means for controlling each means based on the output of a pressure sensor for measuring the pressure in the treatment tank,
Among the pressure steaming that steams the ingredients with the inside of the treatment tank at a pressure higher than the atmospheric pressure and the vacuum steaming that steams the ingredients with the pressure inside the treatment tank at a pressure lower than the atmospheric pressure, the selected steaming can be performed,
After the air is removed from the inside of the processing tank, steam is supplied into the processing tank by the steam supply means, and the inside of the processing tank is kept at the desired pressure P1 while cooking the food. Performing the operation of returning to the desired pressure P1 after depressurization until one or more times,
The desired pressure P1 and the set pressure P2 can be changed,
The pressure in the treatment tank up to the set pressure P2 is such that at least the steaming means is used among the steaming means and the pressure reducing means during the pressure steaming, while the pressure reducing means is used during the steaming under reduced pressure. Using
The return pressure from the set pressure P2 to the desired pressure P1 is performed by supplying steam into the processing tank using the steaming means,
The set pressure P2 is a pressure at which a saturated steam temperature lower than the food material temperature is obtained, and is a pressure in which the temperature difference between the decompressed saturated steam temperature and the food material temperature is within a set range. apparatus.
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JP5754839B2 (en) * 2011-02-02 2015-07-29 株式会社サムソン Steaming device
JP5754838B2 (en) * 2011-02-02 2015-07-29 株式会社サムソン Steaming device
JP5658596B2 (en) * 2011-02-26 2015-01-28 株式会社サムソン Steaming device
JP6419009B2 (en) * 2015-03-31 2018-11-07 エスペック株式会社 Cooker and cooking method
JP6496657B2 (en) * 2015-11-27 2019-04-03 エスペック株式会社 Cooker and cooking method
JP6836943B2 (en) * 2017-03-27 2021-03-03 東芝ホームテクノ株式会社 rice cooker
JP6851298B2 (en) * 2017-10-26 2021-03-31 三菱電機株式会社 Cooker
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JPH0751161A (en) * 1993-08-20 1995-02-28 Matsushita Electric Ind Co Ltd Automatic rice cooker
JPH11244143A (en) * 1998-02-27 1999-09-14 Ono Shokuhin Kogyo Kk Heating cooking sterilizing device
JP2005052048A (en) * 2003-08-01 2005-03-03 Okayama Prefecture Method for producing physiologically active substance or functional food

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0751161A (en) * 1993-08-20 1995-02-28 Matsushita Electric Ind Co Ltd Automatic rice cooker
JPH11244143A (en) * 1998-02-27 1999-09-14 Ono Shokuhin Kogyo Kk Heating cooking sterilizing device
JP2005052048A (en) * 2003-08-01 2005-03-03 Okayama Prefecture Method for producing physiologically active substance or functional food

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