JP2019205518A - Steaming device and heating treatment method - Google Patents

Steaming device and heating treatment method Download PDF

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JP2019205518A
JP2019205518A JP2018101333A JP2018101333A JP2019205518A JP 2019205518 A JP2019205518 A JP 2019205518A JP 2018101333 A JP2018101333 A JP 2018101333A JP 2018101333 A JP2018101333 A JP 2018101333A JP 2019205518 A JP2019205518 A JP 2019205518A
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steam
temperature
confectionery
storage chamber
edible
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JP6457685B1 (en
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健 塩入
Takeshi Shioiri
健 塩入
治 小室
Osamu Komuro
治 小室
盛二 山田
Moriji Yamada
盛二 山田
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Masdac Machinery Co Ltd
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Abstract

To provide a steaming device and a heating treatment method for reducing unevenness in temperature distribution in a storage chamber for storing a processed object.SOLUTION: A steaming machine 1 comprises: an outlet 11 having a check valve 12 so that low temperature ambient air does not reversely flow into a storage chamber, below a mount area 19 for mounting confectionery and other edible object in the storage chamber 10; and an air feeding hole 13 comprising a check valve so as to prevent flowing of high temperature steam in the storage chamber, above the mount area for mounting the confectionery and other edible object in the storage chamber. When the inside of the storage chamber is heated to a temperature less than 100°C, the control part controls temperature by intermittent switching of supply and cut off of the steam at 100°C or higher, and performs exhaustion from the outlet in supply of the steam, and introduces the ambient air from the air feeding hole in cut off of the steam, thereby holding a prescribed pressure.SELECTED DRAWING: Figure 1

Description

本発明は、蒸し機及び加熱処理方法に関し、特に菓子その他可食物の処理温度を100℃未満に維持したときでも収容室下方に備えた排気口からの大気の逆流を防止しつつ収容室上方に備えた給気口から外気を導入することで収容室内の温度分布のばらつきを低減する蒸し機及び加熱処理方法に関する。   The present invention relates to a steamer and a heat treatment method, and in particular, even when the processing temperature of confectionery and other edible substances is maintained below 100 ° C., while preventing backflow of air from the exhaust port provided below the storage chamber, above the storage chamber. The present invention relates to a steamer and a heat treatment method that reduce variation in temperature distribution in a storage chamber by introducing outside air from an air supply port provided.

饅頭や蒸しパンなど蒸気を利用して調理する加工食品は、小規模であれば蒸し器とせいろを使用して手軽に作ることができ、広く普及している。また一度に大量の加熱処理を行う業務用の蒸し機も様々なものが開発され、古くから活用されている。
こうした業務用の蒸し機としては、トンネル内に蒸気を充満させ、その中を被加工物である菓子その他可食物を連続搬送するトンネル式蒸し機と、多段のラックに載置した菓子その他可食物を収容室に設置し、収容室に蒸気を供給して加熱処理を行うバッチ式などの密閉式の蒸し機とがある。
Processed foods cooked using steam, such as buns and steamed bread, can be easily made using steamers and steamers if they are small, and are widely used. In addition, various types of commercial steamers that perform a large amount of heat treatment at once have been developed and used for a long time.
These steamers for business use include a tunnel-type steamer that fills the tunnel with steam and continuously conveys confectionery and other edible foods, and confectionery and other edible foods placed in a multi-stage rack. Is installed in a storage chamber, and there is a batch-type steamer such as a batch type in which steam is supplied to the storage chamber and heat treatment is performed.

トンネル式蒸し機は装置も大型化しやすく、処理能力も高いことから大量生産に適している。一方密閉式の蒸し機は設置面積もトンネル式蒸し機に比べて小さく、又加熱する品種の切り替えも容易であるなど扱いやすいため活用範囲が広い。
密閉式の蒸し機は多段のラックを収容するため、一般的に収容室は縦型であり、その処理能力を上げるためには縦に長くなることから、収容室内の温度分布のばらつきが問題となりやすい。
Tunnel-type steamers are suitable for mass production due to their large size and high processing capacity. On the other hand, the closed steamer has a smaller installation area than the tunnel steamer, and it is easy to handle, such as easy switching of the variety to be heated.
Since a closed steamer accommodates multi-stage racks, the accommodation chamber is generally a vertical type, and in order to increase its processing capacity, it is lengthened vertically. Therefore, variation in temperature distribution in the accommodation chamber becomes a problem. Cheap.

特許文献1には、底付近に設けられた排気口と、底付近に配設されるスパージ管へ蒸気を供給する蒸気供給部と、外気を強制供給又は内部の蒸気を循環する送風機とを備え、対向する側壁の内部に中空部を設けるとともに、内側壁面に無数の蒸気流入口及び流出口を穿設して蒸気が庫内を循環するようにして内部の温度を均一化する蒸し庫が開示されている。   Patent Document 1 includes an exhaust port provided near the bottom, a steam supply unit that supplies steam to a sparge pipe disposed near the bottom, and a blower that forcibly supplies outside air or circulates internal steam. Also disclosed is a steamer in which hollow portions are provided inside the opposing side walls, and innumerable steam inlets and outlets are formed in the inner wall surface so that the steam circulates in the chamber and the internal temperature is made uniform. Has been.

100℃以上の蒸気で加熱し続ける加熱処理方法の場合は、庫内即ち収容室内の蒸気を循環させることで温度分布のばらつきの低減が期待できるが、多くの蒸し菓子では始めから高温で加熱処理を行うと、表面のみが蒸成が進行してしまい、内部への熱が伝わりにくくなってしまうために蒸し状態にむらができたり表面状態がきれいな仕上がりになりにくかったりなどの問題が起こりやすい。そこで内部まで均一に熱が入りやすいように、100℃未満の温度でゆっくり加熱することが、製品品質に大きく影響する。   In the case of a heat treatment method in which heating is continued with steam of 100 ° C. or higher, it is expected that variation in temperature distribution can be reduced by circulating the steam in the storage room, that is, in the storage chamber. If this is done, only the surface will be steamed, and it will be difficult for heat to be transferred to the inside, so that problems such as unevenness in the steamed state and difficulty in achieving a clean finish on the surface are likely to occur. Therefore, slowly heating at a temperature of less than 100 ° C. so as to make it easy for heat to enter evenly inside greatly affects the product quality.

密閉式の蒸し機の場合、通常100℃以上の蒸気で加熱処理を行うため、100℃未満の温度で温度制御を行う場合、蒸気の供給と遮断の繰り返しによって収容室内に入る熱量を制御して所定の温度になるように調整を行う必要がある。このため100℃未満の温度制御はばらつきが起きやすいという課題がある。   In the case of a closed steamer, heat treatment is usually performed with steam at 100 ° C. or higher. When temperature control is performed at a temperature lower than 100 ° C., the amount of heat entering the storage chamber is controlled by repeated supply and shut-off of steam. It is necessary to make adjustments so as to reach a predetermined temperature. For this reason, the temperature control of less than 100 ° C. has a problem that variations easily occur.

蒸気による加熱の場合、蒸気が被加熱物の表面で凝縮する凝縮伝熱により、高い熱伝達率での伝熱が行われる。加熱開始時に蒸気が空気で満たされた収容室内に供給されると、蒸気と空気との混合気体となるが、同じ圧力下では蒸気はその分圧分しか伝熱に寄与できない。即ち収容室内が蒸気で充満された状態に比べ、伝熱の効率が低下する。そこで蒸気より重い空気を、供給する蒸気で置換する必要があり、排気口を収容室の下部に配置することが行われる。   In the case of heating with steam, heat transfer with a high heat transfer rate is performed by condensation heat transfer in which the steam condenses on the surface of the object to be heated. When steam is supplied into the housing chamber filled with air at the start of heating, it becomes a mixed gas of steam and air. However, under the same pressure, steam can contribute only to the partial pressure. That is, the efficiency of heat transfer is reduced as compared with a state in which the accommodation chamber is filled with steam. Therefore, it is necessary to replace air heavier than the steam with the supplied steam, and an exhaust port is disposed in the lower part of the storage chamber.

伝熱に使用された蒸気は凝縮により水となって体積が収縮するため、蒸気の供給を遮断した状態では収容室内の圧力が低下する。特に100℃未満の温度に制御する場合、繰り返し蒸気の遮断が行われるので、圧力低下も繰り返し発生しやすい。こうした凝縮による収容室内の圧力低下は非常に短時間で発生し、それに伴い排気口からの大気の逆流が発生する。このため収容室下方では温度の低い空気の逆流により温度の低下が発生しやすいという課題も認められている。こうした部分的な温度の低下は、多段のラックの下段の方に載置した菓子その他可食物の加熱不足をひきおこすことにもなり、場合によっては多段のラックの下段の方を使用しないように制限が必要となることも起こり得る。   Since the steam used for heat transfer becomes water due to condensation and its volume shrinks, the pressure in the storage chamber decreases in the state where the supply of steam is cut off. In particular, when controlling to a temperature of less than 100 ° C., the steam is repeatedly shut off, so that the pressure drop is likely to occur repeatedly. The pressure drop in the storage chamber due to such condensation occurs in a very short time, and accompanying this, a backflow of air from the exhaust port occurs. For this reason, the subject that the fall of temperature tends to generate | occur | produce by the backflow of the low temperature air under the storage chamber is also recognized. This partial drop in temperature can cause underheating of confectionery and other edible foods placed in the lower part of a multi-stage rack, and in some cases, the lower part of the multi-stage rack is restricted from being used. May be necessary.

このように従来技術では、特に100℃未満の温度に制御する場合の凝縮に伴う圧力低下に対して十分な対策が取られておらず、また温度制御の難しい100℃未満の温度域において収容室内の温度分布を均一化するための対応も十分に行われていなかった。
様々な加工食品が開発され、蒸し機による加熱処理レシピも多様化する中、100℃未満の加熱処理が安定して行え、しかも簡単な構造で収容室内の温度分布のばらつきを抑え、処理能力の低下を招かない蒸し機の提供が望まれる。
As described above, in the prior art, sufficient measures are not taken against the pressure drop due to condensation particularly when the temperature is controlled to be lower than 100 ° C., and in the temperature range lower than 100 ° C. where temperature control is difficult, In order to make the temperature distribution of the film uniform, no sufficient measures have been taken.
While various processed foods have been developed and the heat treatment recipes with steamers are diversifying, heat treatment at less than 100 ° C can be performed stably, and with a simple structure, variation in temperature distribution in the storage chamber can be suppressed, and processing capacity can be improved. It is desirable to provide a steamer that does not cause a drop.

特開平11−000266号公報JP 11-000266 A

本発明は、上記従来の蒸し機における問題点に鑑みてなされたものであって、本発明の目的は、菓子その他可食物の処理温度を100℃未満に維持したときでも収容室下方に備えた排気口からの大気の逆流を防止しつつ収容室上方に備えた給気口から外気を導入することで収容室内の温度分布のばらつきを低減する蒸し機及び加熱処理方法を提供することにある。   The present invention has been made in view of the above problems in the conventional steamer, and the object of the present invention is provided below the storage chamber even when the processing temperature of confectionery and other edible substances is maintained below 100 ° C. It is an object of the present invention to provide a steamer and a heat treatment method that reduce variation in temperature distribution in a storage chamber by introducing outside air from an air supply port provided above the storage chamber while preventing a backflow of air from the exhaust port.

上記目的を達成するためになされた本発明による蒸し機は、蒸気の供給を制御して温度を制御する制御部と、菓子その他可食物の搬入搬出扉と蒸気の供給口とを備えた収容室とを有し、収容室内に載置した菓子その他可食物に蒸気を供給しながら加熱して加工する蒸し機であって、前記収容室は、収容室内の菓子その他可食物の載置エリアより下方に、低温の外気が収容室内に逆流しないように逆止弁を備えた排気口と、収容室内の菓子その他可食物の載置エリアより上方に、収容室内の高温の蒸気が流出しないように逆止弁を備えた給気口とを備え、収容室内を100℃未満に加熱する場合、制御部により100℃以上の蒸気の供給と遮断の断続的な切換により温度制御が行われ、蒸気の供給時には排気口より排気が行われ、蒸気の遮断時には給気口から外気を導入することで所定の圧力を保つことを特徴とする。   A steamer according to the present invention, which has been made to achieve the above object, includes a control unit for controlling the temperature by controlling the supply of steam, a loading / unloading door for confectionery and other edible foods, and a steam supply port. And a steamer that heats and processes the confectionery and other edible food placed in the storage room while supplying steam to the confectionery and other edible food. In order to prevent low-temperature outside air from flowing back into the storage room, the exhaust port provided with a check valve and the high-temperature steam in the storage room are prevented from flowing out above the confectionery or edible placement area in the storage room. When the accommodation chamber is heated to less than 100 ° C., temperature control is performed by intermittent switching between supplying and shutting off the steam at 100 ° C. or higher by the control unit. Sometimes exhaust is performed from the exhaust port and when steam is shut off It is characterized by maintaining a predetermined pressure by introducing outside air from the air supply port.

前記排気口に接続される排気管と前記給気口に接続される給気管とをさらに備え、排気管と給気管とを隣接させる、若しくは給気管又は排気管の一方が他方を貫通する二重管構造とすることにより排気管内の排気により給気管内の給気を加熱することが好ましい。   The exhaust pipe further includes an exhaust pipe connected to the exhaust port and an air supply pipe connected to the air supply port, and the exhaust pipe and the air supply pipe are adjacent to each other, or one of the air supply pipe and the exhaust pipe penetrates the other. It is preferable that the air supply in the air supply pipe is heated by the exhaust in the exhaust pipe by adopting a pipe structure.

上記目的を達成するためになされた本発明による加熱処理方法は、蒸気の供給を制御して温度を制御する制御部と、菓子その他可食物の搬入搬出扉と蒸気の供給口を備えた収容室とを有し、収容室内に載置した菓子その他可食物に蒸気を供給しながら加熱して加工する蒸し機による加熱処理方法であって、収容室内に100℃以上の蒸気を供給して収容室内に載置された菓子その他可食物を収容室内が設定温度に到達するまで加熱する段階と、設定温度に到達後、所定の時間収容室内が設定温度を維持するように制御する段階と、を有し、前記設定温度を維持するように制御する段階は、100℃以上の蒸気を供給する段階と、蒸気の供給を遮断する段階と、を含み、制御部は所定の時間内で蒸気を供給する段階と蒸気の供給を遮断する段階とを選択的に実行することを繰り返し、上記100℃以上の蒸気を供給する段階には収容室内の菓子その他可食物の載置エリアより下方に設けられ、低温の外気が収容室内に逆流しないように逆止弁を備えた排気口より排気が行われ、上記蒸気の供給を遮断する段階には収容室内の菓子その他可食物の載置エリアより上方に設けられ、収容室内の高温の蒸気が流出しないように逆止弁を備えた給気口から外気が導入されることにより収容室内の圧力が保たれることを特徴とする。   The heat treatment method according to the present invention made to achieve the above object includes a control unit that controls the supply of steam to control the temperature, a confectionery and other edible loading / unloading door, and a supply chamber for steam. A steaming machine that heats and processes while supplying steam to confectionery or other edible food placed in the storage chamber, and supplies steam at 100 ° C. or higher to the storage chamber. Heating the confectionery or other edible food placed in the storage room until it reaches the set temperature, and controlling to maintain the set temperature for a predetermined time after reaching the set temperature. The step of controlling so as to maintain the set temperature includes a step of supplying steam at 100 ° C. or higher and a step of shutting off the supply of steam, and the control unit supplies the steam within a predetermined time. Stage and stage to shut off steam supply In the step of supplying the steam at 100 ° C. or higher, it is provided below the confectionery or other edible placement area in the storage chamber so that the low temperature outside air does not flow back into the storage chamber. Exhaust is performed from an exhaust port equipped with a check valve, and at the stage of shutting off the supply of steam, it is provided above the confectionery and other edible placement area in the storage room, and high-temperature steam in the storage room does not flow out. Thus, the pressure in the storage chamber is maintained by introducing outside air from an air supply port provided with a check valve.

本発明に係る蒸し機によれば、菓子その他可食物を100℃未満の温度で加熱処理する場合、蒸気の供給と遮断を繰り返して温度制御を行うが、蒸気を供給して加熱を行う状態では、収容室下方に設けた排気口から収容室下方に滞留する空気を効果的に排気し、蒸気の供給を遮断する状態では逆止弁により排気口からの低温の外気の逆流を防止しつつ収容室上方に備えた給気口から外気を導入することで、蒸気より重い空気による、上方の温度の高い蒸気の、下方への対流が誘発されるので、収容室内の温度分布が均一化され、部分的な温度低下を防止することができる。   According to the steamer according to the present invention, when confectionery or other edible food is heat-treated at a temperature of less than 100 ° C., the temperature is controlled by repeatedly supplying and shutting off the steam. In the state where the air staying below the storage chamber is effectively exhausted from the exhaust port provided below the storage chamber and the supply of steam is shut off, the check valve is used to prevent backflow of low-temperature outside air from the exhaust port. By introducing the outside air from the air supply port provided above the room, the convection of the steam having a higher temperature due to the air heavier than the steam is induced downward, so that the temperature distribution in the accommodation room is made uniform, A partial temperature drop can be prevented.

本発明の実施形態による蒸し機の構造を概略的に示す図である。It is a figure showing roughly the structure of the steamer by the embodiment of the present invention. 本発明の実施形態による蒸し機の構造を概略的に示す平面図である。It is a top view which shows roughly the structure of the steamer by embodiment of this invention. 本発明の他の実施形態による蒸し機の構造を概略的に示す図である。It is a figure which shows roughly the structure of the steamer by other embodiment of this invention. 本発明の実施形態による加熱処理方法を説明するためのフローチャートである。It is a flowchart for demonstrating the heat processing method by embodiment of this invention. 本発明の実施形態による加熱処理における設定温度維持の制御方法を説明するためのフローチャートである。It is a flowchart for demonstrating the control method of preset temperature maintenance in the heat processing by embodiment of this invention.

次に、本発明に係る蒸し機を実施するための形態の具体例を、図面を参照しながら詳細に説明する。
図1は、本発明の実施形態による蒸し機の構造を概略的に示す図である。
図1を参照すると本発明の実施形態による蒸し機1は、菓子その他可食物70を収容する収容室10、蒸気を発生させるボイラー30、蒸気の圧力を下げる減圧弁40、更に低圧の蒸気を発生させる超低圧2次蒸気発生装置50、及び発生した蒸気の供給と遮断を制御して収容室10内の温度を制御する制御部20とを有する。
Next, the specific example of the form for implementing the steamer which concerns on this invention is demonstrated in detail, referring drawings.
FIG. 1 is a diagram schematically illustrating the structure of a steamer according to an embodiment of the present invention.
Referring to FIG. 1, a steamer 1 according to an embodiment of the present invention generates a storage room 10 for storing confectionery and other edible foods 70, a boiler 30 for generating steam, a pressure reducing valve 40 for reducing the pressure of steam, and further generating low pressure steam. An ultra-low pressure secondary steam generator 50 to be controlled, and a control unit 20 that controls supply and shut-off of the generated steam to control the temperature in the storage chamber 10.

本発明による蒸し機は、100℃以上の蒸気の供給と遮断を制御して収容室内の温度を制御し、収容室内に搬入された多段のラックに載置した複数の菓子その他可食物を、所定の温度と時間で蒸気により加熱して蒸し上げる装置である。
図1は、正面の搬入搬出扉を省略し、収容室10内に複数の菓子その他可食物70を載置した多段のラック60が搬入された状態を正面から見て模式的に示す。ラック60は菓子その他可食物70の載置エリア19内に、複数段に菓子その他可食物70を載置し、一度に多数の菓子その他可食物70を蒸すことを可能にする。
The steamer according to the present invention controls the supply and shut-off of steam at 100 ° C. or higher to control the temperature in the storage room, and provides a plurality of confectionery and other edible foods placed in a multistage rack carried into the storage room. It is a device that heats and steams with steam at the temperature and time.
FIG. 1 schematically shows a state in which a multi-stage rack 60 in which a plurality of confectionery and other edible foods 70 are placed in the storage chamber 10 is carried from the front, with the front loading / unloading door omitted. The rack 60 places the confectionery and other edible foods 70 in a plurality of stages in the placement area 19 of the confectionery and other edible foods 70, and makes it possible to steam many confectionery and other edible foods 70 at a time.

また、蒸し機1は、収容室の温度を蒸気の遮断の頻度が高くなる100℃未満に保持する際、蒸気を供給する過程では、蒸気の供給を利用して収容室内の低温の空気又は空気と蒸気の混合気体を収容室外に排気する一方、蒸気の供給を遮断する過程では、蒸気の凝縮に伴う体積低下によって引き起こされる圧力低下に対して、流入する外気を利用して収容室内に自然対流を生じさせ、収容室内の局所的な温度低下を防止するとともに温度の均一化を図ることを可能にする装置である。   In addition, when the steamer 1 keeps the temperature of the storage chamber below 100 ° C. at which the frequency of shutting off the steam is high, in the process of supplying the steam, the steam supply is used to supply low-temperature air or air in the storage chamber. In the process of shutting off the supply of steam while exhausting the mixed gas of steam and steam to the outside of the containment chamber, natural convection is made using the outside air that flows in against the pressure drop caused by the volume drop caused by the condensation of the steam. This is a device that makes it possible to prevent the local temperature drop in the storage chamber and make the temperature uniform.

このため収容室10の下方の底面近傍には、収容室10内の低温の空気又は空気と蒸気の混合気体を収容室10外に排気する排気口11を備える。また収容室10の上方の天板近傍に圧力低下の際に外気を導入する給気口13を備える。   For this reason, an exhaust port 11 for exhausting the low-temperature air in the storage chamber 10 or a mixed gas of air and steam to the outside of the storage chamber 10 is provided near the bottom surface below the storage chamber 10. In addition, an air supply port 13 is provided near the top plate above the storage chamber 10 for introducing outside air when the pressure drops.

初めに複数の菓子その他可食物70を載置した多段のラック60が搬入された時点では、収容室10内は空気で満たされている。加熱が始まり、蒸気が供給されると、比重の関係で、空気より軽い蒸気は収容室10上方に向かいやすく、空気は収容室10下方に集まりやすい。しかし両者は気体同士なので容易に混合し、多くは混合気体として存在する。   When the multistage rack 60 on which a plurality of confectionery and other edible foods 70 are first loaded is loaded, the interior of the storage chamber 10 is filled with air. When heating is started and steam is supplied, steam lighter than air tends to move upward in the accommodation chamber 10 and air tends to gather under the accommodation chamber 10 due to the specific gravity. However, since they are gases, they are easily mixed, and many exist as mixed gases.

蒸気による加熱では、蒸気が保有する熱量が、被加熱物の表面に接触して凝縮することにより被加熱物に伝達される。空気と蒸気の混合気体においても、混合気体中の蒸気が被加熱物の加熱に寄与する。混合気体中の蒸気の比率、即ち蒸気の分圧が低いと加熱に寄与する熱量が少なく、加熱効率が悪い。このため極力空気を排除して蒸気の分圧を上げることが加熱効率の向上につながる。そこで蒸し機1の稼働温度において空気が蒸気より重いこと、また空気にしても混合気体にしても温度の低い状態は温度の高い状態より密度が高く下方に滞留しやすいことなどから、収容室10の下方、特に収容室10内の菓子その他可食物70の載置エリア19より下方に、排気口11を備える。   In heating with steam, the amount of heat held by the steam is transferred to the heated object by contacting the surface of the heated object and condensing. Even in a mixed gas of air and steam, the steam in the mixed gas contributes to the heating of the object to be heated. When the ratio of the vapor in the mixed gas, that is, the partial pressure of the vapor is low, the amount of heat contributing to heating is small and the heating efficiency is poor. For this reason, eliminating the air as much as possible and increasing the partial pressure of the steam leads to an improvement in heating efficiency. Therefore, because the air is heavier than the steam at the operating temperature of the steamer 1, and the low temperature state of both the air and the mixed gas has a higher density than the high temperature state and tends to stay downward. The exhaust port 11 is provided below, in particular, below the placement area 19 for the confectionery and other edible material 70 in the storage chamber 10.

蒸気の供給により収容室10内が所定の保持温度に達すると、制御部20は収容室10内に設けた温度センサの出力に基づき、蒸気の供給と遮断を断続的に切換えて所定の保持温度を維持するように制御する。このとき蒸気を供給している間は、蒸気の供給に伴い排気口11から低温の空気又は混合気体が排気される。しかし、蒸気の供給を遮断している間は排気口11からの排気は行われなくなる。一方この間も蒸気による凝縮が継続して行われるため、凝縮伝熱に寄与した蒸気は水になりその分、体積が低下して、収容室10内の圧力が低下する。圧力が低下すると蒸気温度も低下してしまうので、圧力を維持するために外気の導入が必要となる。従来技術のように収容室10の下方に排気口11を開口させたままの状態だと、収容室10内の圧力低下に伴い排気口11から外気が逆流することになる。温度も低く蒸気より重い逆流した外気はそのまま収容室10の下方に滞留しやすく、収容室10内下方の温度低下をもたらす。   When the inside of the storage chamber 10 reaches a predetermined holding temperature due to the supply of steam, the controller 20 intermittently switches between supply and shut-off of the steam based on the output of the temperature sensor provided in the storage chamber 10 to a predetermined holding temperature. Control to maintain. At this time, while supplying steam, low-temperature air or mixed gas is exhausted from the exhaust port 11 with the supply of steam. However, exhaust from the exhaust port 11 is not performed while the supply of steam is shut off. On the other hand, since the condensation by the steam is continuously performed during this time, the steam contributing to the condensation heat transfer becomes water, and the volume is reduced correspondingly, and the pressure in the storage chamber 10 is lowered. When the pressure decreases, the steam temperature also decreases. Therefore, it is necessary to introduce outside air in order to maintain the pressure. If the exhaust port 11 remains open below the storage chamber 10 as in the prior art, the outside air flows backward from the exhaust port 11 as the pressure in the storage chamber 10 decreases. Outside air having a low temperature and heavier than steam tends to stay in the lower part of the storage chamber 10 as it is, causing a temperature drop in the lower part of the storage chamber 10.

蒸し機1は、こうした従来技術の課題を解決するため、排気口11には逆止弁12を設ける。排気口11の逆止弁12は、排気に対しては弁が開いた状態を維持し、逆流が起ころうとするときに弁を閉じて逆流を防止する。蒸し機1では、収容室10内の圧力低下に対しては別に設けた給気口13から外気を導入する。給気口13は収容室10内の菓子その他可食物70の載置エリア19より上方に備えられる。   The steamer 1 is provided with a check valve 12 at the exhaust port 11 in order to solve such problems of the prior art. The check valve 12 at the exhaust port 11 keeps the valve open for exhaust, and closes the valve to prevent backflow when backflow is about to occur. In the steamer 1, outside air is introduced from an air supply port 13 provided separately for a pressure drop in the storage chamber 10. The air supply opening 13 is provided above the placement area 19 for the confectionery and other edible food 70 in the accommodation room 10.

縦型の収容室10では、収容室10内の雰囲気を循環させる手段を設けないと、上方の温度が高く、下方の温度が低くなる温度分布が生じやすい。特に蒸気の供給が止まる蒸気の遮断状態ではこのような傾向が生じやすくなる。蒸し機1では、蒸気の遮断状態での圧力低下に伴い上方に設けられた給気口13から導入される外気が、収容室10内に比べて温度が低く、また蒸気より重い空気であることから、収容室10内に導入されると収容室10の下方に向かう下降流を形成する。下降流は周囲の温度の高い蒸気を巻き込みながら下降するため、低温の気体が滞留しやすい収容室10の下方に新たな熱量をもたらす。この結果収容室10内の温度分布が改善され、より均一な状態となる。   In the vertical storage chamber 10, if a means for circulating the atmosphere in the storage chamber 10 is not provided, a temperature distribution in which the upper temperature is high and the lower temperature is low is likely to occur. Such a tendency is likely to occur particularly in a steam shut-off state in which the supply of steam is stopped. In the steamer 1, the outside air introduced from the air supply port 13 provided above the pressure drop in the steam shutoff state is lower in temperature than the inside of the housing chamber 10 and is heavier than the steam. Then, when introduced into the storage chamber 10, a downward flow toward the lower side of the storage chamber 10 is formed. The descending flow descends while entraining steam having a high ambient temperature, and therefore brings a new amount of heat below the storage chamber 10 where low-temperature gas tends to stay. As a result, the temperature distribution in the storage chamber 10 is improved and a more uniform state is obtained.

このように蒸し機1では、特別な循環手段を設けることなく、したがって特別な費用をかけることなく、導入される空気の温度差、比重差を利用して収容室10内の温度均一化を図ることができる。
実施形態では最上段の菓子その他可食物70と給気口13との間には屋根型の蒸気反射板18が設けられ、圧力低下に伴い導入される低温の空気が、直接最上段の菓子その他可食物70に降り注ぐことはない。これにより局所的に温度が低下して蒸し上がりにむらが出ることを防止する。
As described above, in the steamer 1, the temperature in the housing chamber 10 is made uniform by utilizing the temperature difference and specific gravity difference of the introduced air without providing any special circulation means and therefore without any special cost. be able to.
In the embodiment, a roof-type vapor reflector 18 is provided between the uppermost confectionery or other edible 70 and the air inlet 13, and the low-temperature air introduced as the pressure decreases is directly applied to the uppermost confectionery or the like. It never falls on edible 70. This prevents the temperature from lowering locally and causing unevenness in steaming.

給気口13も開口させたままにしておくと、収容室10内の圧力が低下するときに外気を導入する働きをする一方、蒸気が供給される状態では、逆に加熱のために供給した蒸気が給気口13から流出してしまうことになる。そこで蒸し機1の給気口13には逆止弁12が設けられる。給気口13の逆止弁12は、給気に対しては弁が開いた状態を維持し、収容室10から蒸気が流出しようとするときに弁を閉じて流出を防止する。   If the air supply port 13 is also left open, it serves to introduce outside air when the pressure in the storage chamber 10 decreases, while it is supplied for heating in a state where steam is supplied. Steam will flow out from the air inlet 13. Therefore, a check valve 12 is provided at the air supply port 13 of the steamer 1. The check valve 12 of the air supply port 13 maintains a state in which the valve is open with respect to the air supply, and closes the valve to prevent outflow when steam is about to flow out of the storage chamber 10.

蒸し機1のボイラー30は、収容室10内を所望の温度に加熱する蒸気を生成できればよく、特に限定はないが実施形態では蒸気量100〜250kg/h、圧力0.3MPaの1次蒸気が供給できるものを使用する。
減圧弁40は1次蒸気のままでは蒸し機に使用するには温度が高すぎるため、1次蒸気の圧力を減圧して、収容室10の加熱に使用しやすい温度の蒸気を生成させる。実施形態では0.01MPa〜0.03MPaの蒸気を生成するように構成される。
超低圧2次蒸気発生装置50は、減圧弁40で生成した蒸気をさらに減圧した湿り蒸気を生成する。この湿り蒸気は蒸成する菓子その他可食物70のボリュームや色つやなどに影響を与えるものである。実施形態では0.003MPa〜0.01MPaの蒸気を生成するように構成される。
The boiler 30 of the steamer 1 is not particularly limited as long as it can generate steam that heats the inside of the housing chamber 10 to a desired temperature. Use what you can supply.
Since the pressure of the pressure reducing valve 40 is too high to be used in a steamer as it is with the primary steam, the pressure of the primary steam is reduced to generate steam having a temperature that is easy to use for heating the storage chamber 10. The embodiment is configured to generate steam of 0.01 MPa to 0.03 MPa.
The ultra-low pressure secondary steam generator 50 generates wet steam obtained by further reducing the pressure of the steam generated by the pressure reducing valve 40. This wet steam affects the volume and color of steamed confectionery and other edible foods 70. The embodiment is configured to generate steam of 0.003 MPa to 0.01 MPa.

制御部20は減圧弁40で生成された蒸気と超低圧2次蒸気発生装置50とを蒸成する菓子その他可食物70の種類や加熱条件に応じて切り換えて収容室10に供給し、仕上がり品質の良い製品を蒸成する。
制御部20にはタッチパネルを兼ねた表示板が備えられ、菓子その他可食物70に応じて加熱プログラムが選択可能に表示され、またそれぞれのプログラムも調整モードを選択することで、減圧弁40からの蒸気と超低圧2次蒸気発生装置50からの湿り蒸気を切り替えるタイミングなどを細かく調整できるように表示する。
The control unit 20 switches the steam generated by the pressure reducing valve 40 and the ultra-low pressure secondary steam generator 50 according to the type and heating conditions of the confectionery and other edible substances 70 that are steamed, and supplies them to the storage chamber 10 for the finished quality. Steaming good products.
The control unit 20 is provided with a display panel that also serves as a touch panel, and a heating program can be selected in accordance with the confectionery and other edible foods 70, and each program also selects an adjustment mode, so that the pressure from the pressure reducing valve 40 is displayed. The timing for switching the steam and the wet steam from the ultra-low pressure secondary steam generator 50 is displayed so that it can be finely adjusted.

図2は、本発明の実施形態による蒸し機の構造を概略的に示す平面図である。
図2では収容室10は説明のために天板を取り除いて、収容室10内が見えるように示す図である。
図2を参照すると、図1では省略した搬入搬出扉16が正面側(図2では下方)に示される。搬入搬出扉16は丁番により収容室10を囲む側壁に固定され、搬入搬出扉16を閉めた状態では丁番を取り付けた側壁と対向する側壁に設けられた回動可能なレバーにより、収容室10内が陽圧になった場合でも開かないようにロックされる。
FIG. 2 is a plan view schematically showing the structure of the steamer according to the embodiment of the present invention.
In FIG. 2, the storage chamber 10 is a view showing the interior of the storage chamber 10 with the top plate removed for explanation.
Referring to FIG. 2, the loading / unloading door 16 omitted in FIG. 1 is shown on the front side (downward in FIG. 2). The loading / unloading door 16 is fixed to the side wall surrounding the storage chamber 10 by a hinge, and when the loading / unloading door 16 is closed, the loading / unloading door 16 is provided by a pivotable lever provided on the side wall facing the side wall to which the hinge is attached. Even if the inside of 10 becomes a positive pressure, it is locked so as not to open.

回動可能なレバーが設けられた側壁には、逆止弁12を備えた排気口11と逆止弁12を備えた給気口13がそれぞれ設けられる。図2では排気口11は搬入搬出扉16から離れた奥側の下方に設けられ、給気口13は収容室10の奥行き方向の中間部に設けられるように示すが、場所や設置数はこれに限らない。排気口11や給気口13はそれぞれ対向する側壁に設けてもよいし、背面の側壁に設けてもよい。さらに、給気口13は収容室10の天板を貫通するように設けてもよい。また排気口11や給気口13はそれぞれ側壁に沿って複数設けてもよい。   An exhaust port 11 provided with a check valve 12 and an air supply port 13 provided with a check valve 12 are provided on the side wall provided with a rotatable lever. In FIG. 2, the exhaust port 11 is provided on the lower side away from the loading / unloading door 16, and the air supply port 13 is illustrated as being provided in the middle in the depth direction of the storage chamber 10. Not limited to. The exhaust port 11 and the air supply port 13 may be provided on opposite side walls, or may be provided on the rear side wall. Furthermore, the air supply port 13 may be provided so as to penetrate the top plate of the storage chamber 10. A plurality of exhaust ports 11 and air supply ports 13 may be provided along the side walls.

また図2では排気口11はL字状の形状を有し、給気口13はT字状の形状を有し、特に給気口13では圧力低下によって導入された外気が奥側と搬入搬出扉16側の2方向に振り分けて流入されるように示したが、これらの形状や長さもこの図の形態とは限らず、排気口11や給気口13は単純に直線的なI字状でも、他の形状でもよい。   In FIG. 2, the exhaust port 11 has an L-shape, and the air supply port 13 has a T-shape. In particular, the external air introduced by the pressure drop is carried in and out of the air supply port 13. Although it is shown that the flow is distributed in two directions on the door 16 side, these shapes and lengths are not limited to those shown in this figure, and the exhaust port 11 and the air supply port 13 are simply linear I-shaped. However, other shapes are possible.

給気口13の下方には蒸気反射板18が設けられる。図1を併せて参照すると、蒸気反射板18は正面側から見て山形の形状を有し、アルミニウムやステンレスの板を曲げ加工して形成される。図1に示すように、ラック60には菓子その他可食物70が複数段に設置されるが、蒸気反射板18はそれぞれの段の菓子その他可食物70を上下から挟み込むように複数が設置される。このような構成とすることにより、それぞれの段の菓子その他可食物70は、上下の蒸気反射板18と収容室10の左右の側壁で囲まれた個別の空間に設置された形となる。   A vapor reflecting plate 18 is provided below the air supply port 13. Referring also to FIG. 1, the vapor reflecting plate 18 has a mountain shape when viewed from the front side, and is formed by bending an aluminum or stainless steel plate. As shown in FIG. 1, the rack 60 is provided with a plurality of confectionery and other edible foods 70, and a plurality of vapor reflectors 18 are provided so as to sandwich the confectionery and other edible foods 70 at each stage from above and below. . By setting it as such a structure, the confectionery and other edible material 70 of each step | paragraph become the form installed in the separate space enclosed by the upper and lower vapor | steam reflector 18 and the left and right side walls of the storage chamber 10.

ボイラー30で形成され減圧弁40や超低圧2次蒸気発生装置50で減圧された蒸気は、配管を通して蒸し機1の背面側に誘導され、ここで正面側から見て左右2本の蒸気パイプ17に分配される。蒸気パイプ17は収容室10内の左右の隔壁に沿って延長され、延長方向には所定の間隔で蒸気を供給する蒸気供給口が開口する。図1に示すように、蒸気パイプ17は、菓子その他可食物70が載置される段ごとに左右に配置される。
菓子その他可食物の載置エリア19は収容室10内の温度の安定性の良い空間域で設定されるが、蒸気パイプ17は、菓子その他可食物の載置エリア19をカバーするように配置する。
The steam formed by the boiler 30 and decompressed by the pressure reducing valve 40 or the ultra-low pressure secondary steam generator 50 is guided to the back side of the steamer 1 through the piping, and here, the two steam pipes 17 on the left and right as viewed from the front side. Distributed to. The steam pipe 17 is extended along the left and right partition walls in the storage chamber 10, and a steam supply port for supplying steam at a predetermined interval opens in the extending direction. As shown in FIG. 1, the steam pipe 17 is arrange | positioned at right and left for every stage in which the confectionery and other edible food 70 are mounted.
The confectionery and other edible placement area 19 is set in a space where the temperature in the storage room 10 is stable, and the steam pipe 17 is arranged to cover the confectionery and other edible placement area 19. .

蒸気パイプ17の蒸気供給口はすぐ下方に位置する下側の蒸気反射板18の上面に向かって蒸気を供給するように開口される。蒸気反射板18の上面に向かって供給された蒸気は蒸気反射板18の上面で反射され、菓子その他可食物70を載置する金網状の載置板を通過して菓子その他可食物70に供給される。
このように菓子その他可食物70が載置される段ごとに個別の空間が割り当てられ、その空間ごとに蒸気供給口が設けられるため、蒸成条件を細かく調整しやすく製品の品質バラツキの低減に有効な構造となっている。
The steam supply port of the steam pipe 17 is opened so as to supply steam toward the upper surface of the lower steam reflecting plate 18 located immediately below. The steam supplied toward the upper surface of the vapor reflecting plate 18 is reflected by the upper surface of the vapor reflecting plate 18, passes through a wire net-like mounting plate on which the confectionery and other edible material 70 is placed, and is supplied to the confectionery and other edible material 70. Is done.
In this way, a separate space is allocated to each stage on which the confectionery or other edible food 70 is placed, and a steam supply port is provided for each space, so that it is easy to finely adjust the steaming conditions and reduce product quality variation. It has an effective structure.

実施形態では収容室10の左右の隔壁に沿って延長される左右の蒸気パイプ17は収容室10の側壁に固定され、菓子その他可食物70の上下を挟み込む蒸気反射板18は専用のラック60に設置されるが、蒸気反射板18は収容室10の側壁に取り付けられてもよく、この場合、菓子その他可食物70を載置する金網状の載置板を蒸気パイプ17の配置ピッチに合わせて複数設置したラック60を用いて菓子その他可食物70の搬入搬出を行う。金網状の載置板を蒸気パイプ17の配置ピッチを併せることにより、ラック60を搬入した状態で載置板に載置した菓子その他可食物70は上下に隣接する2つの蒸気反射板18の間に位置するように搬入される。   In the embodiment, the left and right steam pipes 17 extending along the left and right partition walls of the storage chamber 10 are fixed to the side walls of the storage chamber 10, and the steam reflector 18 sandwiching the top and bottom of confectionery and other edible food 70 is attached to a dedicated rack 60. Although installed, the vapor reflecting plate 18 may be attached to the side wall of the storage chamber 10, and in this case, a wire mesh-like mounting plate on which the confectionery or other edible material 70 is placed is matched with the arrangement pitch of the steam pipes 17. A plurality of racks 60 are used to carry in and out confectionery and other edible foods 70. By combining the arrangement pitch of the steam pipes 17 with the wire mesh-like placement plate, the confectionery and other edible food 70 placed on the placement plate in the state where the rack 60 is carried in between the two vapor reflectors 18 adjacent to each other vertically. It is carried in so that it may be located in.

また複数の蒸気反射板18の内、最上段の菓子その他可食物70と給気口13との間に設置される最上段の蒸気反射板18のみを収容室10に設置し、それ以外の蒸気反射板18は専用のラック60に設置されるようにしてもよい。さらには最上段の蒸気反射板18と給気口13との間に専用の遮蔽板を設け、蒸気反射板の有無にかかわらず給気口13から供給される外気が直接上段の菓子その他可食物70に向けて供給されることの無いようにしてもよい。   Of the plurality of vapor reflectors 18, only the uppermost vapor reflector 18 installed between the uppermost confectionery or other edible 70 and the air supply port 13 is installed in the storage chamber 10, and the other vapors. The reflector 18 may be installed in a dedicated rack 60. Further, a dedicated shielding plate is provided between the uppermost steam reflector 18 and the air inlet 13 so that the outside air supplied from the air inlet 13 is directly on the upper confectionery or other edible matter regardless of the presence or absence of the steam reflector. It may not be supplied to 70.

図3は、本発明の他の実施形態による蒸し機の構造を概略的に示す図である。
図3を参照すると蒸し機2は、制御部20、ボイラー30など蒸気を発生させて温度を制御する要素は図1の蒸し機1と変わらない。蒸し機2が蒸し機1と相違するのは、蒸し機2が排気口11に接続される排気管14と給気口13に接続される給気管15とをさらに備えることである。
蒸し機2は、排気管14と給気管15とを隣接させる、若しくは排気管14又は給気管15の一方が他方を貫通する二重管構造とすることにより、排気管14内の排気により給気管15内の給気を加熱する。
FIG. 3 is a view schematically showing the structure of a steamer according to another embodiment of the present invention.
Referring to FIG. 3, the steamer 2 is the same as the steamer 1 of FIG. 1 in terms of controlling the temperature by generating steam, such as the control unit 20 and the boiler 30. The steamer 2 is different from the steamer 1 in that the steamer 2 further includes an exhaust pipe 14 connected to the exhaust port 11 and an air supply pipe 15 connected to the air supply port 13.
The steamer 2 has a double pipe structure in which the exhaust pipe 14 and the air supply pipe 15 are adjacent to each other, or one of the exhaust pipe 14 and the air supply pipe 15 penetrates the other, so that the air supply pipe is exhausted by the exhaust in the exhaust pipe 14. The supply air in 15 is heated.

蒸し機1は、蒸気の供給を遮断した状態では流入する外気を利用して収容室10内に自然対流を生じさせ、収容室10内温度の均一化を図るが、例えば冬季や寒冷地に設置する場合など、導入される外気の温度が低すぎると、外気が流入する部分やそれに伴う下降流の通過する部分で局所的に温度が下がりすぎ、菓子その他可食物70の蒸し上がり状態に影響を及ぼすことも起こり得る。   When the steam supply is shut off, the steamer 1 generates natural convection in the storage room 10 using the outside air that flows in, and makes the temperature in the storage room 10 uniform. For example, the steaming machine 1 is installed in winter or in a cold region. If the temperature of the outside air to be introduced is too low, the temperature is locally lowered at the part where the outside air flows in or the part where the downward flow passes through it, and the steaming state of the confectionery or other edible food 70 is affected. It can happen.

蒸し機2では排気口11から排気される空気又は混合気体の熱を利用して、給気口13から供給される空気の温度を高める。これにより例えば10℃以下の寒冷な外気の時でも20℃前後の適切な温度にした上で収容室10内に流入させることができる。季節により寒暖差が激しい条件下に設置される場合は排気口11または給気口13の少なくとも一方に排気又は給気の流路を切り替える切換え弁をさらに設け、例えば温度が上昇する季節には排気口11から直接排気するか給気口13から直接給気するようにし、温度が低下する季節にはそれぞれ排気管14を介して排気し、給気管15を介して給気するようにしてもよい。このような切換は手動でもよいし、制御部20の設定により外気温をモニターして外気温に応じて自動的に切り替わるように切換え弁を制御してもよい。   In the steamer 2, the temperature of the air supplied from the air supply port 13 is increased using the heat of the air or mixed gas exhausted from the exhaust port 11. Thereby, even in the case of cold outside air of 10 ° C. or less, for example, the temperature can be adjusted to an appropriate temperature of about 20 ° C. and flowed into the storage chamber 10. When the system is installed under a condition in which the temperature difference varies greatly depending on the season, at least one of the exhaust port 11 and the air supply port 13 is further provided with a switching valve for switching the flow path of the exhaust gas or the air supply port. The air may be exhausted directly from the port 11 or directly from the air supply port 13, and may be exhausted through the exhaust pipe 14 and supplied through the air supply pipe 15 in the season when the temperature decreases. . Such switching may be performed manually, or the switching valve may be controlled so that the outside air temperature is monitored by the setting of the control unit 20 and is automatically switched according to the outside air temperature.

図4は、本発明の実施形態による加熱処理方法を説明するためのフローチャートである。
図4を参照すると、段階S100にて蒸し機1のオペレータは、収容室10内に菓子その他可食物70を載置する。実施形態のように収容室10内に蒸気パイプ17が複数段に設けられている場合は、蒸気パイプ17のピッチに合わせて設置された載置板を備える専用のラック60を利用することにより、菓子その他可食物70は均一な蒸し条件となるように載置することができる。
FIG. 4 is a flowchart for explaining a heat treatment method according to an embodiment of the present invention.
Referring to FIG. 4, in step S <b> 100, the operator of the steamer 1 places confectionery and other edible food 70 in the accommodation room 10. When the steam pipes 17 are provided in a plurality of stages in the storage chamber 10 as in the embodiment, by using a dedicated rack 60 having a mounting plate installed in accordance with the pitch of the steam pipes 17, The confectionery and other edible food 70 can be placed so as to have uniform steaming conditions.

段階S110にて、蒸し機1の制御部20はボイラー30で生成し減圧弁40で減圧した100℃以上の蒸気を供給して、収容室10内が所定の設定温度になるように加熱を開始する。
制御部20は収容室10内に設置した温度センサからの出力を監視し、収容室10内が設定温度に到達したかどうかを判断する(段階S120)。収容室10内が設定温度に到達すると次の収容室10内を設定温度に維持する段階(段階S130)に移行し、設定温度に到達していなければ蒸気の供給による加熱を継続する。
In step S110, the control unit 20 of the steamer 1 supplies steam of 100 ° C. or higher generated by the boiler 30 and depressurized by the pressure reducing valve 40, and starts heating so that the inside of the storage chamber 10 reaches a predetermined set temperature. To do.
The controller 20 monitors the output from the temperature sensor installed in the storage chamber 10 and determines whether or not the interior of the storage chamber 10 has reached the set temperature (step S120). When the inside of the storage chamber 10 reaches the set temperature, the process proceeds to a step of maintaining the next storage chamber 10 at the set temperature (step S130). If the set temperature has not been reached, heating by supplying steam is continued.

図5は、本発明の実施形態による加熱処理における設定温度維持の制御方法を説明するためのフローチャートであり、図4の収容室10内を設定温度に維持する段階の詳細を示す図である。
図5を参照すると、段階S131にて制御部20は、供給していた蒸気を遮断する。前の段階、即ち図4の段階S120にて収容室10内は設定温度に到達しているため、それ以上に温度が上昇しないように蒸気の供給を遮断する。
FIG. 5 is a flowchart for explaining the control method for maintaining the set temperature in the heat treatment according to the embodiment of the present invention, and is a diagram showing details of the stage of maintaining the inside of the storage chamber 10 in FIG. 4 at the set temperature.
Referring to FIG. 5, in step S131, the control unit 20 blocks the supplied steam. In the previous stage, that is, in step S120 of FIG. 4, since the inside of the storage chamber 10 has reached the set temperature, the supply of steam is shut off so that the temperature does not rise any further.

次に制御部20は収容室10内に設置した温度センサからの出力を監視し、収容室10内が設定温度を下回ったかどうかを判断する(段階S132)。収容室10内の温度が設定温度を維持していると判断する場合は蒸気の遮断を維持する。この間収容室10内は蒸気を遮断する前まで供給されていた蒸気が充満した状態にあり、凝縮による熱伝達が継続的に行われる。凝縮された蒸気は水になることで体積が急激に減少し、これに伴って生ずる収容室10内の圧力低下により外気が導入されることになる。   Next, the controller 20 monitors the output from the temperature sensor installed in the storage chamber 10 and determines whether or not the interior of the storage chamber 10 has fallen below the set temperature (step S132). When it is determined that the temperature in the storage chamber 10 maintains the set temperature, the steam is shut off. During this time, the interior of the storage chamber 10 is in a state of being filled with the steam supplied before the steam is shut off, and heat transfer by condensation is continuously performed. Since the condensed steam becomes water, the volume is rapidly reduced, and external air is introduced due to a pressure drop in the storage chamber 10 caused by this.

外気は収容室10の菓子その他可食物の載置エリア19よりも上方に設置された給気口13から導入され、温度も低く蒸気よりも比重が大きいため収容室10内に下降流による自然対流を生じさせる。この間、収容室10の菓子その他可食物の載置エリア19よりも下方に設置された排気口11からは逆止弁12の効果により外気が流入することがない。このため蒸気の供給がなく対流が生じにくい間でも温度分布のばらつきを低減することができる。   The outside air is introduced from an air supply port 13 installed above the confectionery or other edible placement area 19 in the storage room 10 and has a lower temperature and a higher specific gravity than steam. Give rise to During this time, outside air does not flow from the exhaust port 11 installed below the confectionery or other edible placement area 19 in the storage chamber 10 due to the effect of the check valve 12. For this reason, variation in temperature distribution can be reduced even when there is no supply of steam and convection hardly occurs.

一方、段階S132にて収容室10内の温度が設定温度を下回ったと判断すると制御部20は段階S133にて100℃以上の蒸気を供給して加熱する。
100℃以上の蒸気の供給は段階S134にて収容室10内の温度が設定温度以上になったと判断されるまで継続される。100℃以上の蒸気が供給される間、排気口11からは収容室10内でも比較的温度が低い空気、又は空気と蒸気の混合気体が排気される。このとき、給気口13の逆止弁12は蒸気の流出を防止するように閉じられているので、温度の高い蒸気が給気口13から流出することはない。
On the other hand, when it is determined in step S132 that the temperature in the storage chamber 10 has fallen below the set temperature, the controller 20 supplies and heats steam at 100 ° C. or higher in step S133.
The supply of steam at 100 ° C. or higher is continued until it is determined in step S134 that the temperature in the storage chamber 10 has become equal to or higher than the set temperature. While steam of 100 ° C. or higher is supplied, air having a relatively low temperature or a mixed gas of air and steam is exhausted from the exhaust port 11 even in the housing chamber 10. At this time, since the check valve 12 of the air supply port 13 is closed so as to prevent the outflow of steam, high temperature steam does not flow out of the air supply port 13.

制御部20はこのような蒸気の遮断と供給のサイクルを、段階S135で設定時間が終了したと判断されるまで繰り返す。
特に供給する蒸気が100℃以上であるのに対し、収容室10内を100℃未満に維持しようとすると頻繁に蒸気の供給を遮断することが生じ得るが、このような場合でも逆止弁12を備えた排気口11及び給気口13を適切な位置に設けることにより収容室10内の温度分布のばらつきを低減する蒸し機1の提供が可能となる。
The controller 20 repeats such a steam shutoff and supply cycle until it is determined in step S135 that the set time has expired.
In particular, while the supplied steam is 100 ° C. or higher, the supply of the steam may be frequently interrupted if the interior of the storage chamber 10 is maintained below 100 ° C. Even in such a case, the check valve 12 By providing the exhaust port 11 and the air supply port 13 provided with appropriate positions, it is possible to provide the steamer 1 that reduces variations in temperature distribution in the storage chamber 10.

再び図4を参照して、収容室10内を設定温度に維持する段階S130の終了後、蒸気の供給を止め取り出し温度まで降温させ(段階S140)、最終的に段階S150にて加熱処理が終了した菓子その他可食物70を取り出す。   Referring to FIG. 4 again, after the end of step S130 for maintaining the interior of the storage chamber 10 at the set temperature, the supply of steam is stopped and the temperature is lowered to the temperature (step S140), and finally the heat treatment ends in step S150. Take out the confectionery and other edible food 70.

以上、密閉式の蒸し機の中でも、ラックに載置した菓子その他可食物を収容室内に搬入し、まとめて加熱して加工するバッチ式の蒸し機を代表として説明したが、100℃以上の蒸気の供給と遮断により温度制御を行い、菓子その他可食物の搬入搬出時以外は扉を閉めて密閉した収容室内で加熱処理を行う蒸し機についても、逆止弁を備えた給気口を菓子その他可食物の載置エリアの上方に設け、逆止弁を備えた排気口を菓子その他可食物の載置エリアの下方に設けることにより、上記で説明したのと同様の効果を得ることができる。   As described above, a batch type steamer that carries confectionery and other edible foods placed on a rack into a storage room and heats and processes them as a representative among hermetic steamers has been described. For steamers that perform temperature control by supplying and shutting off, and heat-treating in a closed storage room with the door closed except when carrying in / out confectionery and other edible food By providing the edible placement area above the edible placement area and providing the exhaust port provided with the check valve below the confectionery or other edible placement area, the same effect as described above can be obtained.

例えば、1段分の菓子その他可食物を載置した載置板を収容室下方の搬入扉から順次間欠的に収容室内に搬入し、収容室内では加熱処理の進行に合わせて順次上方に移動し、最上段まで移動した時点で加熱処理が終了して搬出扉から順次搬出される垂直型の連続蒸し機についても、搬入搬出時以外は搬入搬出扉を閉めて加熱するので、蒸気の供給を遮断する温度制御時に凝縮伝熱による圧力低下が発生することに変わりはない。この際、下方の排気口は逆止弁により閉じられ、上方の吸気口から外気が導入されるので、導入した外気による下降流により温度分布の均一化が促進されるのである。   For example, a loading plate on which one stage of confectionery or other edible food is placed is intermittently carried into the accommodation chamber sequentially from the carry-in door below the accommodation chamber, and is sequentially moved upward in accordance with the progress of the heat treatment in the accommodation chamber. Also, for vertical continuous steamers that have been heated up when they have moved to the top stage and are sequentially carried out from the carry-out door, the steam supply is shut off because the carry-in / out door is closed and heated except during carry-in and carry-out. However, there is no change in the pressure drop due to condensation heat transfer during temperature control. At this time, the lower exhaust port is closed by the check valve, and the outside air is introduced from the upper intake port, so that the downward flow caused by the introduced outside air promotes uniform temperature distribution.

以上、本発明の実施形態について図面を参照しながら詳細に説明したが、本発明は、上述の実施形態に限定されるものではなく、本発明の技術的範囲から逸脱しない範囲内で多様に変更することが可能である。   As mentioned above, although embodiment of this invention was described in detail, referring drawings, this invention is not limited to the above-mentioned embodiment, In the range which does not deviate from the technical scope of this invention, it changes variously. Is possible.

1、2 蒸し機
10 収容室
11 排気口
12 逆止弁
13 給気口
14 排気管
15 給気管
16 搬入搬出扉
17 蒸気パイプ
18 蒸気反射板
19 菓子その他可食物の載置エリア
20 制御部
30 ボイラー
40 減圧弁
50 超低圧2次蒸気発生装置
60 ラック
70 菓子その他可食物
DESCRIPTION OF SYMBOLS 1, 2 Steamer 10 Accommodating room 11 Exhaust port 12 Check valve 13 Supply port 14 Exhaust pipe 15 Supply tube 16 Carry-in / out door 17 Steam pipe 18 Steam reflector 19 Placement area for confectionery and other food 20 Control unit 30 Boiler 40 Pressure reducing valve 50 Ultra-low pressure secondary steam generator 60 Rack 70 Confectionery and other edible foods

Claims (3)

蒸気の供給を制御して温度を制御する制御部と、菓子その他可食物の搬入搬出扉と蒸気の供給口とを備えた収容室とを有し、収容室内に載置した菓子その他可食物に蒸気を供給しながら加熱して加工する蒸し機であって、
前記収容室は、
収容室内の菓子その他可食物の載置エリアより下方に、低温の外気が収容室内に逆流しないように逆止弁を備えた排気口と、
収容室内の菓子その他可食物の載置エリアより上方に、収容室内の高温の蒸気が流出しないように逆止弁を備えた給気口と、を備え、
収容室内を100℃未満に加熱する場合、制御部により100℃以上の蒸気の供給と遮断の断続的な切換により温度制御が行われ、
蒸気の供給時には排気口より排気が行われ、蒸気の遮断時には給気口から外気を導入することで所定の圧力を保つことを特徴とする蒸し機。
For a confectionery or other edible food that has a control unit for controlling the temperature by controlling the supply of steam, and a storage room having a carry-in / out door for confectionery or other edible food and a supply port for steam. A steamer that heats and processes while supplying steam,
The containment chamber is
An exhaust port provided with a check valve so that low-temperature outside air does not flow back into the storage room below the confectionery or other edible placement area in the storage room;
An air supply port provided with a check valve so that high-temperature steam in the storage room does not flow out from the confectionery or other edible placement area in the storage room;
When heating the storage chamber to below 100 ° C., temperature control is performed by intermittent switching between supply and shutoff of steam at 100 ° C. or higher by the control unit,
A steamer characterized in that when steam is supplied, exhaust is performed from an exhaust port, and when steam is shut off, outside air is introduced from an air supply port to maintain a predetermined pressure.
前記排気口に接続される排気管と前記給気口に接続される給気管とをさらに備え、排気管と給気管とを隣接させる、若しくは給気管又は排気管の一方が他方を貫通する二重管構造とすることにより排気管内の排気により給気管内の給気を加熱することを特徴とする請求項1に記載の蒸し機。   The exhaust pipe further includes an exhaust pipe connected to the exhaust port and an air supply pipe connected to the air supply port, and the exhaust pipe and the air supply pipe are adjacent to each other, or one of the air supply pipe and the exhaust pipe penetrates the other. The steamer according to claim 1, wherein the air supply in the air supply pipe is heated by the exhaust in the exhaust pipe by adopting a pipe structure. 蒸気の供給を制御して温度を制御する制御部と、菓子その他可食物の搬入搬出扉と蒸気の供給口を備えた収容室とを有し、収容室内に載置した菓子その他可食物に蒸気を供給しながら加熱して加工する蒸し機による加熱処理方法であって、
収容室内に100℃以上の蒸気を供給して収容室内に載置された菓子その他可食物を収容室内が設定温度に到達するまで加熱する段階と、
設定温度に到達後、所定の時間収容室内が設定温度を維持するように制御する段階と、を有し、
前記設定温度を維持するように制御する段階は、
100℃以上の蒸気を供給する段階と、
蒸気の供給を遮断する段階と、を含み、
制御部は所定の時間内で蒸気を供給する段階と蒸気の供給を遮断する段階とを選択的に実行することを繰り返し、
上記100℃以上の蒸気を供給する段階には収容室内の菓子その他可食物の載置エリアより下方に設けられ、低温の外気が収容室内に逆流しないように逆止弁を備えた排気口より排気が行われ、
上記蒸気の供給を遮断する段階には収容室内の菓子その他可食物の載置エリアより上方に設けられ、収容室内の高温の蒸気が流出しないように逆止弁を備えた給気口から外気が導入されることにより収容室内の圧力が保たれることを特徴とする加熱処理方法。
It has a control unit for controlling the temperature by controlling the supply of steam, a storage room with a confectionery and other edible loading / unloading door and a steam supply port, and steam is placed on the confectionery and other edible food placed in the storage room. It is a heat treatment method by a steamer that heats and processes while supplying
Heating the confectionery and other edible food placed in the storage chamber by supplying steam at 100 ° C. or higher until the storage chamber reaches a set temperature;
A step of controlling the storage chamber to maintain the set temperature for a predetermined time after reaching the set temperature,
The step of controlling to maintain the set temperature includes:
Supplying steam at 100 ° C. or higher;
Shutting off the supply of steam, and
The controller repeats selectively executing the step of supplying steam and the step of shutting off the supply of steam within a predetermined time,
In the step of supplying steam at 100 ° C. or higher, exhaust is provided from an exhaust port provided below the confectionery and edible placement area in the storage room and provided with a check valve so that low-temperature outside air does not flow back into the storage room. Is done,
At the stage of shutting off the supply of steam, outside air is provided from an air supply port provided above the confectionery or edible placement area in the storage room and provided with a check valve so that high-temperature steam in the storage room does not flow out. A heat treatment method characterized in that the pressure in the accommodation chamber is maintained by being introduced.
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JPH0928565A (en) * 1995-07-17 1997-02-04 Tsuneo Hosogoe Ventilation type low temperature cooking device
JPH11266A (en) * 1997-06-13 1999-01-06 Takagi Kogyo Kk Steaming chamber
JPH11137433A (en) * 1997-11-10 1999-05-25 Goka Chouriki:Kk Large-capacity steamer
JP2005237633A (en) * 2004-02-26 2005-09-08 Miura Co Ltd Steamer
JP2007222314A (en) * 2006-02-22 2007-09-06 Miura Co Ltd Cooking apparatus and cooking method
JP2007229379A (en) * 2006-03-03 2007-09-13 Miura Co Ltd Steam heating apparatus
JP2007268017A (en) * 2006-03-31 2007-10-18 Miura Co Ltd Steam-heating apparatus
JP2015019839A (en) * 2013-07-19 2015-02-02 株式会社井上製作所 Method of heating in-refrigerator food using steam
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JPH0928565A (en) * 1995-07-17 1997-02-04 Tsuneo Hosogoe Ventilation type low temperature cooking device
JPH11266A (en) * 1997-06-13 1999-01-06 Takagi Kogyo Kk Steaming chamber
JPH11137433A (en) * 1997-11-10 1999-05-25 Goka Chouriki:Kk Large-capacity steamer
JP2005237633A (en) * 2004-02-26 2005-09-08 Miura Co Ltd Steamer
JP2007222314A (en) * 2006-02-22 2007-09-06 Miura Co Ltd Cooking apparatus and cooking method
JP2007229379A (en) * 2006-03-03 2007-09-13 Miura Co Ltd Steam heating apparatus
JP2007268017A (en) * 2006-03-31 2007-10-18 Miura Co Ltd Steam-heating apparatus
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