JP2006204808A - Food heating method and apparatus - Google Patents

Food heating method and apparatus Download PDF

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JP2006204808A
JP2006204808A JP2005024476A JP2005024476A JP2006204808A JP 2006204808 A JP2006204808 A JP 2006204808A JP 2005024476 A JP2005024476 A JP 2005024476A JP 2005024476 A JP2005024476 A JP 2005024476A JP 2006204808 A JP2006204808 A JP 2006204808A
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closed space
food
temperature
steam
heating
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JP4588473B2 (en
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Hajime Akasaka
元 赤坂
Takahiro Arai
孝廣 新井
Naohito Okamoto
尚人 岡本
Hideki Miyanishi
秀樹 宮西
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Mayekawa Manufacturing Co
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a heating apparatus finding optimal operating conditions for various types of utilizations such as sterilization, steaming and baking of each foods and allowing the easy setting of the optimal conditions and to suppress the inflow of outside air and the outflow of steam, and to facilitate maintenance such as cleaning and a check of an apparatus inside. <P>SOLUTION: This food heating apparatus is provided with a secondary heating device 10 heating primary steam generated from another heating source by dielectric heating or induction heating and producing secondary high-temperature steam, a plurality of nozzles 17-24 dispersedly disposed in a closed space (s) and supplying the secondary high-temperature steam to the closed space, an exhaust steam circulating passage 13 connecting an exhaust port 29 exhausting exhaust steam from the closed space to the secondary heating device 10, a highly heat-resistant blower 27 interposed in the exhaust steam circulating passage, and valve mechanisms 41 and 41 provided in a channel 12 supplying the primary steam to the secondary heating device 10 and the exhaust steam circulating passage 13 and adjusting the supply ratio of the primary steam. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、150〜300℃の水蒸気により、食品の蒸煮、焼成、食品表面の殺菌、野菜類のブランチングなどの殺菌、調理を行なう加熱装置及び同装置を用いた加熱方法に関し、詳しくは、一般蒸気ボイラなどの加熱装置で製造される一次水蒸気をベースにして、これを誘電加熱又は誘導加熱を用いた二次加熱装置によって二次加熱して高温水蒸気を発生させ、この高温水蒸気を満たした閉空間を食品を載置したコンベアを搬送させることによって行うものであるが、この際食品の殺菌、調理などの目的に応じて運転条件を任意に調節することを可能としたものである。   The present invention relates to a heating apparatus for performing cooking, cooking, baking of food surfaces, sterilization of food products, blanching of vegetables, etc., and a heating method using the same, using steam at 150 to 300 ° C., Based on primary steam produced by a heating device such as a general steam boiler, this was secondarily heated by a secondary heating device using dielectric heating or induction heating to generate high-temperature steam, and this high-temperature steam was filled. This is performed by transporting a conveyor on which food is placed in a closed space. At this time, it is possible to arbitrarily adjust the operating conditions in accordance with the purpose of sterilization and cooking of the food.

従来過熱水蒸気を用いて、食品の焼成、加熱調理、殺菌及び蒸煮等を行う方法及び装置が公知である。
例えば、特許文献1(特開2003−325340号公報)には、常圧の過熱蒸気を用い、この過熱蒸気を循環使用することにより、排気量を少なくして熱効率の向上を図ることができ、焼成コストの低減と省スペース化を可能にする焼成装置が開示されている。
Conventionally, methods and apparatuses for performing baking, heat cooking, sterilization, steaming, and the like of foods using superheated steam are known.
For example, Patent Document 1 (Japanese Patent Laid-Open No. 2003-325340) uses normal pressure superheated steam and circulates and uses this superheated steam, thereby reducing the amount of exhaust and improving thermal efficiency. A firing apparatus that can reduce the firing cost and save space is disclosed.

また特許文献2(特開2004−121431号公報)には、過熱水蒸気噴射ノズルの噴射口の位置を、被加熱物に対して可変とすることにより、過熱水蒸気による加熱温度を調節することができる過熱水蒸気による、食品等の被加熱物の加熱方法及び装置が開示されている。   Moreover, in patent document 2 (Unexamined-Japanese-Patent No. 2004-121431), the heating temperature by superheated steam can be adjusted by making the position of the injection port of a superheated steam injection nozzle variable with respect to a to-be-heated material. A method and apparatus for heating an object to be heated such as food by superheated steam is disclosed.

特開2003−325340号公報JP 2003-325340 A 特開2004−121431号公報JP 2004-121431 A

しかしながらこれら過熱水蒸気を用いた従来の加熱装置には次のような問題点がある。
即ちまず従来の装置は、二次加熱装置にガスや灯油などの燃焼方式を使用しているため、排気ガスの発生が避けられず、また安全性に問題があった。また個々の食品に対して、加熱装置に供給する過熱水蒸気の温度、湿度その他の最適運転条件がまだ見出されていない。例えば食品の表面殺菌にとっては、乾熱より湿熱を利用するほうが効率が良く、食品の品質劣化も最小限にとどめることができるが、このためには閉空間を最適湿度条件に容易に設定できるようにする必要がある。しかし従来の加熱装置では、最適な湿度条件を容易に設定できる手段は未だ提案されていない。
However, these conventional heating devices using superheated steam have the following problems.
That is, first, the conventional apparatus uses a combustion system such as gas or kerosene for the secondary heating apparatus, so that generation of exhaust gas is inevitable and there is a problem in safety. Furthermore, the optimum operating conditions such as the temperature, humidity and other conditions of superheated steam supplied to the heating device have not yet been found for individual foods. For example, for heat sterilization of food, it is more efficient to use wet heat than dry heat, and the quality degradation of food can be minimized. For this purpose, the closed space can be easily set to the optimum humidity condition. It is necessary to. However, the conventional heating apparatus has not yet proposed a means for easily setting the optimum humidity condition.

また食品の蒸煮と焼成の運転方法については、前者は湿度が高く、後者では湿度が低い条件が適するが、食品の種類によっては湿度が高い条件においても焼成が可能であり、これは二次加熱された過熱蒸気の供給量が大きな要因となる。しかしながら未だ湿度と二次過熱蒸気の供給量との関連は明らかにされていない。   As for the operation method of cooking and baking of food, the former is suitable for high humidity and the latter is suitable for low humidity. However, depending on the type of food, baking can be performed under high humidity. The amount of superheated steam supplied is a major factor. However, the relationship between the humidity and the supply amount of secondary superheated steam has not been clarified yet.

また従来加熱装置の庫内温度分布を一定にしようとして、過剰のエネルギーを使用して制御しようとしていた。また食品と過熱蒸気を接触させる閉空間は、食品を載置したコンベアが出入りするため、完全な密閉空間とすることはできず、コンベアの出入り口から蒸気が外部へ流出したり、外部から閉空間へ外気が流入したりして、閉空間の温度コントロールが非常に難しく、通常、入口にノレンを取り付けたりして、外気の進入、蒸気流出を防止していたが、食品にノレンが触れるなどの非衛生的な問題があり、未だこれが解決されていない。   In addition, conventionally, an attempt has been made to control by using excessive energy in order to make the temperature distribution inside the heating apparatus constant. In addition, the closed space where food and superheated steam are brought into contact cannot be made completely sealed because the conveyor on which the food is placed enters and exits, and steam flows out from the entrance / exit of the conveyor or is closed from the outside. It is very difficult to control the temperature of the closed space due to the inflow of outside air. Normally, noren was attached to the inlet to prevent ingress of air and outflow of steam. There are unsanitary issues that have not yet been resolved.

また加熱装置庫内にこびり付いた汚れ、特に油脂類、焦げ付きによるスケールなどについては、装置が洗浄構造となっていないため、水を使用しないで拭き取る、あるいは掏り取るなどのドライ洗浄を主体とした洗浄方法によったため、洗浄洗い残しや臭いなどのこびり付きなどの問題があった。   Also, dirt that sticks in the heating device cabinet, especially oils and fats, and scales due to scorching, are mainly structured by dry cleaning such as wiping or scrubbing without using water because the device does not have a cleaning structure. Due to the cleaning method, there were problems such as residue from cleaning and stickiness such as odor.

本発明は、かかる従来技術の課題に鑑み、安全性に問題がなく、個々の食品の殺菌、蒸煮、焼成などの調理等各種用途に最適な運転条件を見出すとともに、最適な条件設定を容易に行なうことのできる加熱装置を実現し、また閉空間への外気の流入及び閉空間からの蒸気の流出を抑制し、また装置内部の洗浄、点検等のメンテナンスを容易にすることを目的とする。   In view of the problems of the prior art, the present invention has no problem in safety, finds optimum operating conditions for various uses such as sterilization, steaming, baking, etc. of individual foods, and easily sets optimum conditions. An object of the present invention is to realize a heating device that can be performed, to suppress the inflow of outside air into the closed space and the outflow of steam from the closed space, and to facilitate maintenance such as cleaning and inspection inside the device.

本発明の食品加熱装置は、前記目的を達成するため、高耐熱性パネルで囲われた閉空間に、同閉空間を貫く高耐熱性のコンベアで食品を搬送させながら、連続的に加熱する装置において、他の加熱源で発生した水蒸気を誘電加熱又は誘導加熱によって150〜350℃に加熱する二次加熱装置と、前記閉空間に分散配置され同閉空間に前記高温水蒸気を供給する複数のノズルと、同閉空間から排蒸気を排気する排気口と前記加熱装置とを接続する排蒸気循環路と、同排蒸気循環路に介設された高耐熱性ブロアと、前記二次加熱装置に一次水蒸気を供給する流路及び前記排蒸気循環路に設けられ、一次水蒸気の供給割合を調節可能にした弁機構とを備えたことを特徴とする。   In order to achieve the above object, the food heating device of the present invention is a device that continuously heats food in a closed space surrounded by a high heat-resistant panel while conveying the food with a high heat-resistant conveyor that penetrates the closed space. A secondary heating device that heats water vapor generated in another heating source to 150 to 350 ° C. by dielectric heating or induction heating, and a plurality of nozzles that are distributed in the closed space and supply the high-temperature water vapor to the closed space And an exhaust steam circulation path connecting the heating device with an exhaust port for exhausting exhaust steam from the enclosed space, a high heat resistant blower interposed in the exhaust steam circulation path, and a primary to the secondary heating device It is provided with a flow path for supplying water vapor and a valve mechanism provided in the exhaust steam circulation path and capable of adjusting a supply ratio of primary water vapor.

本発明装置において、一次水蒸気を、例えば装置周辺にある工場用ボイラ等を使って製造する。この一次水蒸気を誘電加熱又は誘導加熱法を用いた二次加熱装置によって150〜350℃に加熱し、この二次高温水蒸気を閉空間内で食品と接触させ、加熱して殺菌、調理する。本発明装置は、通常常圧下で食品に蒸気を接触させる。二次加熱装置内でも同様であるが、一次水蒸気が二次加熱装置に高圧で供給される場合もあり、これらの理由により若干の圧力変動はあり得る。
150℃から水蒸気凝縮により食品の初期昇温速度が加速される。水蒸気のもつ熱量は乾熱加熱の8倍であるため、より短時間で調理、殺菌が可能となる。
また本発明装置においては、水蒸気凝縮のみならず、高耐熱パネルによる放射伝熱、及び水蒸気による対流伝熱も加わって、高効率伝熱を可能とする。
In the apparatus of the present invention, primary steam is produced using, for example, a factory boiler around the apparatus. This primary water vapor is heated to 150 to 350 ° C. by a secondary heating device using dielectric heating or induction heating, and this secondary high temperature water vapor is brought into contact with food in a closed space and heated to sterilize and cook. In the apparatus of the present invention, steam is brought into contact with food under normal pressure. The same is true in the secondary heating device, but the primary steam may be supplied to the secondary heating device at a high pressure, and for these reasons, there may be slight pressure fluctuations.
The initial heating rate of the food is accelerated by steam condensation from 150 ° C. Since the amount of heat of water vapor is eight times that of dry heat heating, cooking and sterilization can be performed in a shorter time.
In the apparatus of the present invention, not only water vapor condensation but also radiant heat transfer by a high heat-resistant panel and convective heat transfer by water vapor are added to enable high-efficiency heat transfer.

食品加熱後の排蒸気は前記排気口から前記高耐熱性ブロアによって吸引され、前記排蒸気循環路を経て二次加熱装置に戻され、二次加熱装置で再加熱される。この際一次水蒸気が補充水蒸気として適宜補給されるが、この際前記弁機構により一次水蒸気量及び排蒸気量を調整することができるとともに、両者の混合割合を調節することができる。   The exhaust steam after heating the food is sucked from the exhaust port by the high heat resistance blower, returned to the secondary heating device through the exhaust steam circulation path, and reheated by the secondary heating device. At this time, the primary water vapor is appropriately replenished as supplemental water vapor. At this time, the primary water vapor amount and the exhaust steam amount can be adjusted by the valve mechanism, and the mixing ratio of both can be adjusted.

また本発明装置において、好ましくは、前記コンベアの上下に複数のノズル管を分散配置し、前記閉空間の入口及び出口付近の上方に配置されたノズル管を食品の搬送方向と直角方向に配置したストレート型とするとともに、これらノズル管のノズル開口を真下に向け、前記ストレート型ノズル管以外はループ型とし、コンベアの上方中央部に配置されたループ型ノズル管のノズル開口を前記閉空間の中央側に傾斜させ、下方に配置されたループ型ノズル管のノズル開口を真下に向けるようにする。   In the apparatus of the present invention, preferably, a plurality of nozzle tubes are dispersedly arranged above and below the conveyor, and the nozzle tubes arranged above the entrance and exit of the closed space are arranged in a direction perpendicular to the food conveyance direction. A straight type, and the nozzle openings of these nozzle pipes are directed directly downward, the other than the straight type nozzle pipe is a loop type, and the nozzle opening of the loop type nozzle pipe arranged at the upper central portion of the conveyor is the center of the closed space The nozzle opening of the loop type nozzle tube disposed below is inclined directly downward.

コンベア上面側の入口開口及び出口開口は、コンベア上に載置された食品を出入りさせる必要があるため、開口を大きく取る必要があり、このため外気の流入及び水蒸気の流出が起こりやすい。しかしコンベア上方の入口及び出口付近に配置された前記ストレート型ノズル管から排出される水蒸気のエアカーテン効果により、外部への蒸気の流出及び外部からの外気の流入を防止することができる。
またコンベアの上方中央側に設けられたループ型ノズル管は、閉空間の上方中央部の蒸気雰囲気を一定の温度に保つ役割を果たす。またコンベアの下方に配置されたループ型ノズル管蒸気を真下に吹きつけると、蒸気の性格上吹き付けとほぼ同時に真上に立ち上がり、食品の裏側から包み込むような雰囲気を形成することができる。
The entrance opening and the exit opening on the upper surface side of the conveyor need to allow foods placed on the conveyor to enter and exit. Therefore, it is necessary to make the opening large, so that inflow of outside air and outflow of water vapor are likely to occur. However, the outflow of steam to the outside and the inflow of outside air from the outside can be prevented by the air curtain effect of the steam discharged from the straight type nozzle pipe arranged near the inlet and outlet above the conveyor.
Further, the loop type nozzle tube provided on the upper center side of the conveyor plays a role of maintaining the steam atmosphere in the upper center portion of the closed space at a constant temperature. Further, when the loop type nozzle pipe steam disposed below the conveyor is blown directly down, it is possible to form an atmosphere that rises almost immediately at the same time as the steam and wraps from the back side of the food.

また本発明装置において、好ましくは、前記閉空間を形成する筐体の前記コンベアの長手方向に沿う側壁面に開閉可能な点検扉を設け、同筐体の底面を形成する底板を着脱可能とし、同底板に排水口を設け、同筐体内部を洗浄可能に構成する。これによって、コンベアレール、奥の壁、ノズル管などに手が届くようになり、水、湯を使用した手洗浄を可能とし、さらに底面を形成する底板を着脱可能として、洗浄排水を速やかに庫外に排出できるようになる。なお装置を構成する機器、部材の材質を耐アルカリ性とすれば、アルカリ洗浄あるいは弱酸性洗剤にも対応可能となる。
また本発明装置において、好ましくは、加熱装置本体を収容した筐体の下部にキャスターを設け、同筐体を移動可能にする。
In the apparatus of the present invention, preferably, an inspection door that can be opened and closed is provided on a side wall surface of the casing that forms the closed space along the longitudinal direction of the conveyor, and a bottom plate that forms the bottom surface of the casing is removable. A drain outlet is provided on the bottom plate so that the inside of the housing can be cleaned. This makes it possible to reach the conveyor rail, back wall, nozzle tube, etc., enabling manual cleaning using water and hot water, and detaching the bottom plate that forms the bottom surface to quickly store the cleaning wastewater. It becomes possible to discharge outside. In addition, if the material of the apparatus and member which comprise an apparatus is made into alkali resistance, it will become possible to respond also to an alkali washing or a weak acid detergent.
In the apparatus of the present invention, preferably, a caster is provided at the lower part of the casing that houses the heating apparatus main body so that the casing can be moved.

また本発明方法は、前記構成を有する食品加熱装置において、前記閉空間の温度を検出する温度センサによって閉空間の温度状況をモニタし、このデータ情報に基づいて前記ブロアの回転数を比例制御によって調節することにより、前記閉空間の温度を150〜350℃に制御するとともに、前記二次加熱装置の出口側水蒸気の温度を検出する温度センサにより出口側水蒸気温度をモニタし、このデータ情報に基づいて前記二次加熱装置の出力を比例制御によって調節することにより、同加熱装置の出口側水蒸気の温度を制御する。   In the food heating apparatus having the above-described configuration, the method of the present invention monitors the temperature state of the closed space by a temperature sensor that detects the temperature of the closed space, and proportionally controls the rotation speed of the blower based on this data information. By adjusting, the temperature of the closed space is controlled to 150 to 350 ° C., and the outlet side water vapor temperature is monitored by a temperature sensor that detects the temperature of the outlet side water vapor of the secondary heating device, and based on this data information Then, the temperature of the outlet side steam of the heating device is controlled by adjusting the output of the secondary heating device by proportional control.

また本発明方法において、好ましくは、前記閉空間内で温度センサを前記コンベアで搬送される食品の近傍に設け、食品近傍の温度状況をモニタする。これによって食品近傍の温度状況に基づいて前記ブロアの回転数制御を行なうことができる。
また本発明方法は、好ましくは、食品を蒸煮又は焼成するに際し、一次水蒸気の前記二次加熱装置への供給量及び前記閉空間の温度を調整することにより、前記閉空間の水蒸気の相対湿度を3〜6%RHに制御する。焼成の際は、相対湿度を3%側に設定することが適し、遠赤外線効果も生じて焦げ目を付けることができる。一方、蒸煮の際は、相対湿度を6%側に設定することが適する。
In the method of the present invention, preferably, a temperature sensor is provided in the vicinity of the food conveyed by the conveyor in the closed space, and the temperature condition in the vicinity of the food is monitored. Accordingly, the rotational speed of the blower can be controlled based on the temperature condition in the vicinity of the food.
Further, the method of the present invention preferably adjusts the relative humidity of water vapor in the closed space by adjusting the supply amount of primary water vapor to the secondary heating device and the temperature of the closed space when cooking or baking food. Control to 3-6% RH. At the time of firing, it is suitable to set the relative humidity to 3%, and a far-infrared effect can also be produced, which can be burnt. On the other hand, when cooking, it is suitable to set the relative humidity to the 6% side.

本発明装置によれば、他の加熱源で発生した水蒸気を誘電加熱又は誘導加熱によって150〜350℃に加熱する二次加熱装置と、前記閉空間に分散配置され同閉空間に前記高温水蒸気を供給する複数のノズルと、同閉空間から排蒸気を排気する排気口と前記加熱装置とを接続する排蒸気循環路と、同排蒸気循環路に介設された高耐熱性ブロアと、前記二次加熱装置に一次水蒸気を供給する流路及び前記排蒸気循環路に設けられ、一次水蒸気の供給割合を調節可能にした弁機構とを備えたことにより、水蒸気凝縮のみならず、高耐熱パネルによる放射伝熱、及び水蒸気による対流伝熱も加わって、高効率伝熱を可能とするとともに、排蒸気を循環して使用するため、排蒸気量を少なくして熱効率の向上を図ることができ、加熱コストの低減と省スペース化を可能とする。   According to the apparatus of the present invention, a secondary heating device that heats water vapor generated by another heating source to 150 to 350 ° C. by dielectric heating or induction heating, and the high-temperature water vapor distributed in the closed space are disposed in the closed space. A plurality of nozzles to be supplied; an exhaust port that exhausts exhaust steam from the closed space; and a heat exhaust circuit that connects the heating device; a high heat-resistant blower interposed in the exhaust steam circuit; By providing a flow path for supplying primary steam to the secondary heating device and a valve mechanism for adjusting the supply ratio of primary steam, provided in the exhaust steam circulation path, not only steam condensation but also a high heat-resistant panel In addition to radiant heat transfer and convective heat transfer by steam, it enables high-efficiency heat transfer and circulates and uses exhaust steam, reducing the amount of exhaust steam and improving thermal efficiency. Reduced heating costs To allow space.

また二次加熱装置は、ガスや灯油など燃焼方式を使わないため、安全性が高いとともに、誘電加熱又は誘導加熱を用いた二次加熱装置を用いるため、短時間で加熱が可能となり、150〜350℃の高温水蒸気を使った低酸素状態のため、油脂の酸化を始め、その他食品成分からの酸化物の生成を抑え、ビタミンの破壊が抑制され、加熱処理された食品の保存性が向上し、また食品の退色防止効果を有する。
本発明は、食品の調理、殺菌、ブランチング、野菜、果実の皮むき等に広く適用することができる。
In addition, since the secondary heating device does not use a combustion method such as gas or kerosene, it is highly safe and uses a secondary heating device using dielectric heating or induction heating, so that heating can be performed in a short time, and 150 to Due to the low oxygen state using high-temperature steam at 350 ° C, the oxidation of fats and oils, the generation of oxides from other food ingredients are suppressed, the destruction of vitamins is suppressed, and the preservability of heat-treated foods is improved. In addition, it has the effect of preventing fading of food.
The present invention can be widely applied to food cooking, sterilization, blanching, vegetable peeling, fruit peeling, and the like.

また本発明装置において、好ましくは、前記コンベアの上下に複数のノズル管を分散配置し、前記閉空間の入口及び出口の上方に配置されたノズル管を食品の搬送方向と直角方向に配置したストレート型とするとともに、これらノズル管のノズル開口を真下に向け、前記ストレート型ノズル管以外はループ型とし、コンベアの上方に配置されたループ型ノズル管のノズル開口を前記閉空間の中央側に傾斜させ、下方に配置されたループ型ノズル管のノズル開口を真下に向けるように構成したことにより、連続処理に必要な蒸気流出・外気進入防止の最適化を図ることができ、連続処理・ライン化が容易になるとともに、食品の前面、後面、上面、下面、右面、左面の空間雰囲気を最適条件に設定された均一な高温水蒸気で包むことができる。   In the apparatus of the present invention, preferably, a plurality of nozzle pipes are arranged in a distributed manner above and below the conveyor, and the nozzle pipes arranged above the inlet and outlet of the closed space are arranged in a direction perpendicular to the food conveying direction. The nozzle opening of these nozzle pipes is directly below, and the other than the straight nozzle pipe is a loop type, and the nozzle opening of the loop type nozzle pipe disposed above the conveyor is inclined toward the center of the closed space. In addition, it is possible to optimize the prevention of steam outflow and the entry of outside air necessary for continuous processing by configuring the nozzle opening of the loop type nozzle tube arranged below to be directly below. And the space atmosphere on the front, back, top, bottom, right and left sides of the food can be wrapped with uniform high-temperature steam set to optimum conditions.

また好ましくは、前記閉空間を形成する筐体の前記コンベアの長手方向に沿う側壁面に点検扉を設け、同筐体の底面を形成する底板を着脱可能とし、同底板に排水口を設け、同筐体内部を洗浄可能にしたことによって、コンベアレール、奥の壁、ノズル管などに手が届くようになり、水、湯を使用した手洗浄を可能とし、さらに底面を着脱可能にしたことにより、洗浄排水を速やかに庫外に排出できるようになる。なお装置を構成する機器、部材の材質を耐アルカリ性とすれば、アルカリ洗浄あるいは弱酸性洗剤にも対応可能となる。
また好ましくは、加熱装置本体を収容した筐体の下部にキャスターを設け、同筐体を移動可能にすることにより、ラインのレイアウト変更などの際は、一次蒸気配管などを繋ぎ変えるだけで、任意の場所に移動可能になる。現在多品種少量生産が大きな割合を占め、日ごとあるいは時間ごとのレイアウト変更が盛んに行なわれている。筐体の下部にキャスターを設けたことにより、このようなニーズに対応可能となる。
Preferably, an inspection door is provided on a side wall surface of the casing that forms the closed space along the longitudinal direction of the conveyor, a bottom plate that forms a bottom surface of the casing is detachable, and a drain outlet is provided on the bottom plate. By making the inside of the housing washable, it is possible to reach the conveyor rail, back wall, nozzle tube, etc., enabling manual washing with water and hot water, and making the bottom surface removable. As a result, the washing waste water can be quickly discharged out of the warehouse. In addition, if the material of the apparatus and member which comprise an apparatus is made into alkali resistance, it will become possible to respond also to an alkali washing or a weak acid detergent.
Preferably, a caster is provided at the lower part of the casing containing the heating device main body, and the casing can be moved, so that when changing the layout of the line, it is possible to change the primary steam piping etc. It becomes possible to move to the place. Currently, high-mix low-volume production accounts for a large proportion, and layout changes are being made every day or every hour. By providing a caster at the bottom of the housing, it is possible to meet such needs.

また本発明方法によれば、前記構成を有する食品加熱装置において、前記閉空間の温度を検出する温度センサによって閉空間の温度状況をモニタし、このデータ情報に基づいて前記ブロアの回転数を比例制御によって調節することにより、前記閉空間の温度を150〜350℃に制御するとともに、前記二次加熱装置の出口側水蒸気の温度を検出する温度センサにより出口側水蒸気温度をモニタし、このデータ情報に基づいて前記二次加熱装置の出力を調節することにより、同二次加熱装置の出口側水蒸気の温度を制御することによって、閉空間の水蒸気温度を常に設定された最適な温度に維持することができ、このため個々の食品の各種用途に迅速に対応することができる。
また前記二次加熱装置の出口側水蒸気の温度を制御することによって、二次加熱装置の異常過熱を防ぐことができる。
According to the method of the present invention, in the food heating apparatus having the above configuration, the temperature state of the closed space is monitored by the temperature sensor that detects the temperature of the closed space, and the rotation speed of the blower is proportional to the data information. By adjusting by control, the temperature of the closed space is controlled to 150 to 350 ° C., and the outlet side water vapor temperature is monitored by a temperature sensor that detects the temperature of the outlet side water vapor of the secondary heating device. By adjusting the output of the secondary heating device based on the above, by controlling the temperature of the outlet-side water vapor of the secondary heating device, the water vapor temperature in the closed space is always maintained at the optimum temperature set. Therefore, it is possible to quickly cope with various uses of individual foods.
Moreover, abnormal overheating of the secondary heating device can be prevented by controlling the temperature of the outlet side steam of the secondary heating device.

また本発明方法において、好ましくは、前記閉空間内で温度センサを前記コンベアで搬送される食品の近傍に設け、食品近傍の温度状況をモニタすることによって、食品近傍の温度状況に基づいて前記ブロアの回転数制御を行ない、食品近傍の温度状況を基準に閉空間の雰囲気条件を設定することにより、蒸気の過剰供給を防止し、エネルギーロスを抑えることができる。   In the method of the present invention, preferably, a temperature sensor is provided in the vicinity of the food conveyed by the conveyor in the closed space, and the temperature condition in the vicinity of the food is monitored, so that the blower is based on the temperature condition in the vicinity of the food. By controlling the number of rotations and setting the atmosphere conditions in the closed space based on the temperature conditions in the vicinity of the food, excessive supply of steam can be prevented and energy loss can be suppressed.

また本発明方法において、好ましくは、食品を蒸煮又は焼成するに際し、一次水蒸気の前記二次加熱装置への供給量及び前記閉空間の温度を調整することにより、前記閉空間の水蒸気の相対湿度を3〜6%RHに制御することにより、焼成あるいは蒸煮に好適な相対湿度で加熱処理を行うことができる。   In the method of the present invention, preferably, when steaming or baking the food, the relative humidity of the water vapor in the closed space is adjusted by adjusting the supply amount of the primary water vapor to the secondary heating device and the temperature of the closed space. By controlling to 3 to 6% RH, heat treatment can be performed at a relative humidity suitable for baking or steaming.

以下、本発明を図に示した実施例を用いて詳細に説明する。但し、この実施例に記載されている構成部品の寸法、材質、形状、その相対配置などは特に特定的な記載がない限り、この発明の範囲をそれのみに限定する趣旨ではなく、単なる説明例にすぎない。
図1は、本発明装置の第1実施例の断面立面図、図2は、前記第1実施例の断面平面図、図3は、前記第1実施例の制御系の系統図である。
Hereinafter, the present invention will be described in detail with reference to the embodiments shown in the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the component parts described in this example are not intended to limit the scope of the present invention only to specific examples unless otherwise specified. Only.
FIG. 1 is a sectional elevation view of a first embodiment of the apparatus of the present invention, FIG. 2 is a sectional plan view of the first embodiment, and FIG. 3 is a system diagram of a control system of the first embodiment.

図1〜3において、1は、内部で閉空間を形成している筐体で、基台25によって支持され、コンベアベルト4及びコンベアベルト4上の載置された被加熱食品wが出入りする入口開口2及び出口開口3を有する。なお筐体1の閉空間sを取り巻く内壁は、図示しない高耐熱性パネルで被覆されている。コンベアベルト4は、高耐熱性の材質からなり、入口側従動スプロケット5及び出口側駆動スプロケット6に巻回されて、駆動モータ9により駆動され、コンベアベルト4上に載置された食品wを搬送する。   1-3, 1 is the housing | casing which forms the closed space inside, and is supported by the base 25, and the inlet_port | entrance where the heated food w mounted on the conveyor belt 4 and the conveyor belt 4 enters and exits. It has an opening 2 and an outlet opening 3. The inner wall surrounding the closed space s of the housing 1 is covered with a high heat resistance panel (not shown). The conveyor belt 4 is made of a material having high heat resistance, is wound around the inlet-side driven sprocket 5 and the outlet-side drive sprocket 6, is driven by the drive motor 9, and conveys the food w placed on the conveyor belt 4. To do.

7は、入口側スプロケット5を覆うケーシング、8は、出口側スプロケット6を覆うケーシング、9は出口側駆動スプロケット6を駆動する電動モータである。26は、閉空間sを形成するため、筐体1内を上下に仕切る底板であり、底板26は、筐体1内部の洗浄を容易にするため着脱可能に設けられ、かつ斜めに傾斜しており、傾斜下方側に開閉弁付排水口47を設けている。30は、スプロケット6と駆動モータ9に巻回されたチェーンベルトである。
10は、図3に図示される高周波発生装置11から送られる高周波電流により供給される一次水蒸気に循環電流を誘起させて発熱させることにより一次水蒸気を加熱する二次加熱機である。二次加熱機10には、工場等に設置されたボイラで製造された一次水蒸気が、一次蒸気管路12から循環管路13を経て供給され、二次加熱機10で二次加熱される。高周波発生装置からは、周波数が5〜40kHzの高周波が供給される。
7 is a casing covering the inlet side sprocket 5, 8 is a casing covering the outlet side sprocket 6, and 9 is an electric motor for driving the outlet side driving sprocket 6. Reference numeral 26 denotes a bottom plate that divides the inside of the housing 1 up and down to form a closed space s. The bottom plate 26 is detachably provided to facilitate cleaning of the inside of the housing 1 and is inclined obliquely. In addition, a drain outlet 47 with an on-off valve is provided on the inclined lower side. A chain belt 30 is wound around the sprocket 6 and the drive motor 9.
Reference numeral 10 denotes a secondary heater that heats the primary steam by inducing circulation current in the primary steam supplied by the high-frequency current sent from the high-frequency generator 11 shown in FIG. 3 to generate heat. Primary steam produced by a boiler installed in a factory or the like is supplied to the secondary heater 10 from the primary steam line 12 via the circulation line 13 and is secondarily heated by the secondary heater 10. A high frequency with a frequency of 5 to 40 kHz is supplied from the high frequency generator.

二次加熱機10で二次加熱された一次水蒸気は、150〜350℃の高温水蒸気となって、二次加熱機10の出口側循環管路14を経て、筐体1内の上下で分岐する上部ヘッダ15及び下部ヘッダ16に供給され、さらに上部ヘッダ15に接続された上部ノズル管17,18,19及び20に供給されるとともに、下部ヘッダ16に接続された下部ノズル管21,22,23及び24に供給される。
29は、閉空間s内の上方に設けられた吸引口で、循環管路13に接続され、循環管路13は、途中に一次蒸気管路12が接続され、さらに循環ブロア27が介設され、二次加熱機10に接続されている。28は、循環ブロア27の駆動モータである。また図2において、45は、コンベアベルト4の搬送方向に沿って設けられた点検扉である。
The primary steam secondary-heated by the secondary heater 10 becomes high-temperature steam at 150 to 350 ° C., and branches up and down in the housing 1 through the outlet-side circulation conduit 14 of the secondary heater 10. The lower nozzle pipes 21, 22, and 23 connected to the lower header 16 are supplied to the upper header 15 and the lower header 16, and further supplied to the upper nozzle pipes 17, 18, 19, and 20 connected to the upper header 15. And 24.
Reference numeral 29 denotes a suction port provided above the closed space s, which is connected to the circulation line 13. The circulation line 13 is connected to the primary steam line 12 in the middle, and a circulation blower 27 is interposed. The secondary heater 10 is connected. Reference numeral 28 denotes a drive motor for the circulation blower 27. In FIG. 2, 45 is an inspection door provided along the conveying direction of the conveyor belt 4.

次に第1実施例の制御系を図3及び図4に基づいて説明する。図において、31は、閉空間sに設けられた温度センサで、図4に示すように、温度センサ31の検出値は比較器34に送られて、温度設定器32により設定された設定値と比較され、設定値と検出値との差は比例制御器33によって比例処理され、その比例処理値に基づいて循環ブロア27の回転数を制御する。
また35は、二次加熱機10の出口側循環管路14に設けられた出口部水蒸気温度を検出する温度センサで、図4に示すように、温度センサ35の検出値は比較器37に送られて、温度設定器32により設定された設定値と比較され、設定値と検出値との差は比例制御器36によって比例処理され、その比例処理値に基づいて高周波発生装置11の出力制御(0から100%)を行い、二次加熱機10出口部の水蒸気温度を制御する。
Next, the control system of the first embodiment will be described with reference to FIGS. In the figure, 31 is a temperature sensor provided in the closed space s. As shown in FIG. 4, the detected value of the temperature sensor 31 is sent to the comparator 34, and the set value set by the temperature setter 32. The difference between the set value and the detected value is proportionally processed by the proportional controller 33, and the rotational speed of the circulation blower 27 is controlled based on the proportionally processed value.
Reference numeral 35 denotes a temperature sensor that detects the outlet water vapor temperature provided in the outlet-side circulation pipe 14 of the secondary heater 10, and the detected value of the temperature sensor 35 is sent to the comparator 37 as shown in FIG. The difference between the set value and the detected value is proportionally processed by the proportional controller 36, and output control of the high-frequency generator 11 (based on the proportionally processed value) 0 to 100%) to control the water vapor temperature at the outlet of the secondary heater 10.

また図3において、40は、循環管路13に介設された流量調整弁、41は、一次蒸気管路12に設けられた流量調整弁である。これらの弁を適宜調整することにより、閉空間sから循環される排蒸気及び一次水蒸気の流量のみならず、両者の混合割合を調整することができる。また42は、二次加熱機10内に冷却水を循環管路43及び44を介して循環することにより、二次加熱機10内の加熱盤を冷却するラジエータである。
また46は、筐体1の下部に設けられたキャスターで、基台25を伸縮可能にすることにより、筐体1を所望の場所に移動することができる。
In FIG. 3, 40 is a flow rate adjusting valve provided in the circulation line 13, and 41 is a flow rate adjusting valve provided in the primary steam line 12. By appropriately adjusting these valves, it is possible to adjust not only the flow rates of exhaust steam and primary steam circulated from the closed space s but also the mixing ratio of both. Reference numeral 42 denotes a radiator that cools the heating panel in the secondary heater 10 by circulating cooling water in the secondary heater 10 through circulation lines 43 and 44.
Reference numeral 46 denotes a caster provided at the lower portion of the casing 1, and the casing 1 can be moved to a desired location by making the base 25 extendable and contractible.

かかる第1実施例の装置において、一次水蒸気が閉空間sから排出される排蒸気と混合されて二次加熱機10に供給され、そこで二次加熱されて150〜350℃の設定温度となった高温水蒸気は上部ヘッダ15及び下部ヘッダ16を介してノズル管17〜24に供給される。本装置は、通常常圧下で食品に蒸気を接触させる。二次加熱機10内でも同様であるが、一次水蒸気が二次加熱機10に高圧で供給される場合もあり、これらの理由により若干の圧力変動はあり得る。
コンベアベルト4の上方で筐体1の入口部及び出口部に配置されたノズル管17及び20は、図1および図2に示すように、直線状をなし、ノズル口は真下に向けて配置されているので、水蒸気は矢印a及びdのように真下に噴出し、これによって入口開口2及び出口開口3からのがきの流入及び筐体1内の水蒸気の流出を防止することができる。
In the apparatus of the first embodiment, the primary steam is mixed with the exhaust steam discharged from the closed space s and supplied to the secondary heater 10 where the secondary steam is heated to a set temperature of 150 to 350 ° C. High-temperature steam is supplied to the nozzle tubes 17 to 24 through the upper header 15 and the lower header 16. The apparatus normally contacts the food with steam under normal pressure. Although it is the same also in the secondary heater 10, primary steam may be supplied to the secondary heater 10 at a high pressure, and there may be some pressure fluctuations for these reasons.
As shown in FIGS. 1 and 2, the nozzle pipes 17 and 20 arranged at the inlet and outlet of the housing 1 above the conveyor belt 4 are linear and the nozzle opening is arranged directly below. Therefore, the water vapor is ejected directly below as indicated by arrows a and d, whereby the inflow of postcards from the inlet opening 2 and the outlet opening 3 and the outflow of water vapor in the housing 1 can be prevented.

一方その他のノズル管18,19,21,22,23及び24は、図1および図2に示すように、ループ型をなし、このうちノズル管19は庫内側へ約15度の角度を付けられ、ノズル管18は庫内側へ約345度の角度を付けられており、これによって矢印c及びbのように閉空間sの中央部に向かって蒸気が供給されるので、閉空間s中央部の蒸気雰囲気を一定の温度に保つことができる。
またコンベアベルト4の下部に配置されたノズル管21〜24は、すべてループ型をなし、ノズル開口はすべて真下に向いているので、矢印eからhのように蒸気は真下に向かって噴出するが、食品wの裏面から包み込むような雰囲気を形成する。
このためこれらのノズル管により、食品wの前後、左右、上下の空間を均一な水蒸気で包み込むことができ、加熱処理に最適な雰囲気を維持することができる。
On the other hand, as shown in FIGS. 1 and 2, the other nozzle tubes 18, 19, 21, 22, 23, and 24 have a loop shape. Among these, the nozzle tube 19 is angled by about 15 degrees toward the inner side. The nozzle tube 18 is angled approximately 345 degrees toward the inside of the chamber, and as a result, steam is supplied toward the central portion of the closed space s as indicated by arrows c and b. The steam atmosphere can be maintained at a constant temperature.
In addition, the nozzle pipes 21 to 24 arranged at the lower part of the conveyor belt 4 are all loop-shaped and the nozzle openings are all directed downward, so that the steam is jetted downward as indicated by arrows e to h. An atmosphere that wraps from the back side of the food w is formed.
For this reason, these nozzle tubes can wrap the front and rear, left and right, and upper and lower spaces of the food w with uniform water vapor, and can maintain an optimum atmosphere for the heat treatment.

また本装置には、図2に示すようにコンベアベルト4の搬送方向に沿って開閉可能な点検扉45を設け、筐体1の底面を形成する底板26を着脱可能とし、かつ底板26は斜めに傾斜しており、傾斜下方側に開閉弁付排水口47を設けたことにより、庫内の洗浄、点検等を容易に行うことができる。即ち通常運転時は、コンベアのレールとネットの接触する部分については、ネットの自重によってガイドされ、食品を搬送するが、洗浄時はネットを持ち上げ、接触部分を手洗浄することができる。また庫内の洗浄方法として、一次蒸気を噴霧し、焼成カスや食品から滲み出た油脂類を剥離及び溶解させる。さらに庫内の部材は耐アルカリ性を選定しており、汚れの成分を剥離、溶解後、アルカリ洗剤を噴霧する。次いでスポンジを用いて手洗浄などにより摩擦力で汚れ成分を取る。さらに焼成などにより固化したスケール成分については、酸洗浄し、温水を噴霧して濯ぎ洗いをして完了する。   Further, as shown in FIG. 2, this apparatus is provided with an inspection door 45 that can be opened and closed along the conveying direction of the conveyor belt 4 so that the bottom plate 26 that forms the bottom surface of the housing 1 can be attached and detached. By providing the drain opening 47 with the on-off valve on the lower side of the inclination, the inside of the warehouse can be easily cleaned and inspected. That is, during normal operation, the portion where the rail of the conveyor contacts the net is guided by the weight of the net and transports food, but when cleaning, the net can be lifted and the contact portion can be manually washed. Also, as a cleaning method in the storage, primary steam is sprayed to peel and dissolve the oils and fats exuded from the baking residue and food. Further, the members in the chamber are selected for alkali resistance, and after removing and dissolving the dirt components, an alkaline detergent is sprayed. Next, the sponge is used to remove dirt components by friction, such as by hand washing. Further, the scale component solidified by baking or the like is washed with an acid, rinsed with spray of warm water, and completed.

また閉空間sに温度センサ31を設け、また二次加熱機10の出口側循環路14に温度センサ35を設け、図4に示す制御を行なって、閉空間s内の温度及び二次加熱機10の出口側水蒸気温度を設定温度に保持できるので、食品wの種類及び殺菌、調理等加熱処理の用途に応じて最適の条件設定を行なうことができるとともに、二次加熱機10の異常過熱を未然に防止することができる。なお二次加熱機10においては、ラジエータ42で冷却される冷却水で熱板(図示略)の過熱を効果的に防止することができる。
循環管路13及び一次蒸気管路12に設けた流量調整弁40及び41により、閉空間sから排気される排蒸気及び一次水蒸気の二次加熱機10への供給量及び両者の混合割合を自由に変えることができるので、例えばノズル管への蒸気供給量を多くすることにより、加熱能力を増大することもでき、あるいは両者の混合割合を調整して、相対湿度を3〜6%に調整し、これによって食品の蒸煮あるいは焼成に最適な条件を設定することができる。
In addition, a temperature sensor 31 is provided in the closed space s, and a temperature sensor 35 is provided in the outlet-side circulation path 14 of the secondary heater 10, and the control shown in FIG. 4 is performed to determine the temperature in the closed space s and the secondary heater. 10 outlet-side water vapor temperature can be maintained at the set temperature, so that optimum conditions can be set according to the type of food w and the use of heat treatment such as sterilization and cooking, and abnormal overheating of the secondary heater 10 can be performed. It can be prevented in advance. In the secondary heater 10, overheating of the hot plate (not shown) can be effectively prevented by the cooling water cooled by the radiator 42.
The flow rate adjusting valves 40 and 41 provided in the circulation line 13 and the primary steam line 12 allow free supply of exhaust steam and primary steam exhausted from the closed space s to the secondary heater 10 and the mixing ratio of both. For example, the heating capacity can be increased by increasing the amount of steam supplied to the nozzle tube, or the mixing ratio of both can be adjusted to adjust the relative humidity to 3-6%. This makes it possible to set the optimum conditions for cooking or baking the food.

本実施例の装置においては、ノズル管に供給する蒸気温度を150〜350℃、蒸気循環量を1〜35m/min,コンベア速度を30m/sec,一次水蒸気量を1〜70kg/Hとすることにより、殺菌、調理環境に最適であることを見出した。
このように第1実施例によれば、水蒸気凝縮のみならず、高耐熱パネルによる放射伝熱、及び水蒸気による対流伝熱も加わって、高効率伝熱を可能とするとともに、排蒸気を循環して使用するため、排蒸気量を少なくして熱効率の向上を図ることができ、加熱コストの低減と省スペース化を可能とする。
In the apparatus of this embodiment, the steam temperature supplied to the nozzle tube is 150 to 350 ° C., the steam circulation rate is 1 to 35 m 3 / min, the conveyor speed is 30 m / sec, and the primary water vapor amount is 1 to 70 kg / H. It was found that it is optimal for sterilization and cooking environment.
As described above, according to the first embodiment, not only the steam condensation but also the radiant heat transfer by the high heat-resistant panel and the convection heat transfer by the steam are added to enable high efficiency heat transfer and to circulate the exhaust steam. Therefore, it is possible to reduce the amount of exhaust steam and improve the thermal efficiency, thereby reducing the heating cost and saving space.

また二次加熱機10は、ガスや灯油など燃焼方式を使わないため、安全性が高いとともに、150〜350℃の高温水蒸気を使った低酸素状態のため、油脂の酸化を始め、その他食品成分からの酸化物の生成を抑え、ビタミンの破壊が抑制され、加熱処理された食品の保存性が向上し、また食品の退色防止効果を有する。
なお温度センサ31をコンベアベルト4で搬送される食品Wの近傍に配置すれば、食品近傍の温度状況をモニタすることによって、食品近傍の温度状況に基づいてブロア27の回転数制御を行ない、食品近傍の温度状況を基準に閉空間の雰囲気条件を設定することにより、蒸気の過剰供給を防止し、エネルギーロスを抑えることができる。
また現在多品種少量生産が大きな割合を占め、日ごとあるいは時間ごとのレイアウト変更が盛んに行なわれている。本実施例によれば、筐体1の下部にキャスター46を装着し、筐体1を移動可能にすることにより、ラインのレイアウト変更などの際は、一次蒸気配管などを繋ぎ変えるだけで、任意の場所に移動することができ、頻繁なレイアウト変更に対応することができる。
In addition, the secondary heater 10 does not use a combustion method such as gas or kerosene, so it has high safety and is in a low oxygen state using high-temperature steam at 150 to 350 ° C., so that oxidation of fats and oils and other food components This suppresses the formation of oxides from the food, suppresses the destruction of vitamins, improves the preservability of the heat-treated food, and has the effect of preventing the food from fading.
If the temperature sensor 31 is disposed in the vicinity of the food W transported by the conveyor belt 4, the rotational speed of the blower 27 is controlled based on the temperature in the vicinity of the food by monitoring the temperature in the vicinity of the food. By setting the atmospheric conditions of the closed space based on the temperature conditions in the vicinity, excessive supply of steam can be prevented and energy loss can be suppressed.
In addition, high-mix low-volume production accounts for a large proportion, and layout changes are being made every day or every hour. According to the present embodiment, the caster 46 is attached to the lower part of the housing 1 so that the housing 1 can be moved, so that when the line layout is changed, the primary steam pipe is simply changed. It is possible to move to the location of the location, and to cope with frequent layout changes.

第1実施例の装置を用いて、凍結原料(ハンバーグ用牛肉)の表面殺菌を行なった第2実施例について説明する。
その前段階として、図5は、第1実施例の装置を用いて、閉空間sの雰囲気温度分布を調べた結果を示す。即ち閉空間sの温度を240℃に設定し、その中で温度センサを前後6箇所に取り付けたテストピースを60秒間コンベアベルト上を移動させたときのテストピース表面から10mm付近の雰囲気温度測定結果を示す。図に示すように、テストピース表面から10mm付近の雰囲気は20秒間で200℃に昇温しており、入口付近及び出口付近に設けられたノズル管20及び17によるエアカーテン効果が発揮されていることがわかる。
The second embodiment in which the frozen raw material (hamburger beef) is sterilized using the apparatus of the first embodiment will be described.
As the previous stage, FIG. 5 shows the result of examining the atmospheric temperature distribution in the closed space s using the apparatus of the first embodiment. That is, the temperature of the closed space s is set to 240 ° C., and the ambient temperature measurement result of about 10 mm from the surface of the test piece when the test piece with the temperature sensors attached at the six front and rear positions is moved on the conveyor belt for 60 seconds. Indicates. As shown in the figure, the atmosphere around 10 mm from the surface of the test piece is heated to 200 ° C. in 20 seconds, and the air curtain effect is exerted by the nozzle tubes 20 and 17 provided near the inlet and near the outlet. I understand that.

第2実施例では、閉空間sの温度を200℃に設定し、凍結肉表面温度を装置投入後30秒で80℃に昇温可能とすることを目的として運転した結果を図6の温度グラフに示す。図6は、筐体1の入口から出口までの凍結肉表面温度を測定したもので、図6からほぼ目的が達成されていることがわかる。
このときの菌数(大腸菌群)は、処理前:1.0×10/100cmに対して、処理後:検出されず/100cmであった。
In the second embodiment, the temperature of the closed space s is set to 200 ° C., and the operation result for the purpose of allowing the frozen meat surface temperature to be raised to 80 ° C. in 30 seconds after the introduction of the apparatus is shown in the temperature graph of FIG. Shown in FIG. 6 shows the measurement of the surface temperature of the frozen meat from the entrance to the exit of the housing 1, and it can be seen from FIG. 6 that the object is almost achieved.
Cell count at this time (coliform bacteria) are pretreated: For 1.0 × 10 3 / 100cm 2, after treatment: was not detected / 100 cm 2.

次に前記第1実施例の装置を惣菜(卵焼き)の表面殺菌に適用した第3実施例を説明する。卵焼き表面温度80℃30秒を目的とした場合、庫内温度設定については180℃1分の処理により、菌数(大腸菌群)は、処理前:1.0×10/100cmに対して、処理後:検出されず/100cmであった。また外観は、黄色部分及び焼き目部分ともにほとんど変化がなかった。
図7の(a)は、黄色部分の外観変化を測定したグラフ、(b)は、焼き目部分の外観を測定したグラフである。このグラフは、JIS(JISZ8729)で規定されたL表色系色度図であり、明度をL、色度をa(赤方向)、b(黄色方向)で表す。数値が大きくなるにしたがって色鮮やかになり、視位置が小さくなるにしたがってくすんだ色になる。図7からわかるように、2分経過してもほとんど明度及び色度が変わらないことがわかる。
Next, a description will be given of a third embodiment in which the apparatus of the first embodiment is applied to surface sterilization of sugar beet (eggaki). When intended for omelette surface temperature 80 ° C. 30 seconds, by treatment of 180 ° C. 1 min for internal temperature setting, cell count (coliform bacteria) are pretreated: For 1.0 × 10 3 / 100cm 2 After treatment: not detected / 100 cm 2 . In addition, there was almost no change in the appearance of both the yellow portion and the grilled portion.
(A) of FIG. 7 is a graph which measured the external appearance change of the yellow part, (b) is a graph which measured the external appearance of the burning part. This graph is a chromaticity diagram of L * a * b * color system specified by JIS (JISZ8729), where lightness is represented by L * , chromaticity is represented by a * (red direction), and b * (yellow direction). . The color becomes brighter as the value increases, and the color becomes duller as the viewing position decreases. As can be seen from FIG. 7, the brightness and chromaticity hardly change even after 2 minutes.

次に前記第1実施例の装置を冷凍ハンバーグの加熱・焼成に適用した第4実施例について説明する。庫内温度320℃に設定し、130gのハンバーグで中芯温度90℃1秒仕上げで8分、70gのハンバーグで中芯温度90℃1秒仕上げで5分で完了した。このとき殺菌効果+表面の焼成による焼き目の形成+可食に値する調理が可能であった。   Next, a description will be given of a fourth embodiment in which the apparatus of the first embodiment is applied to heating and baking of a frozen hamburger. The inside temperature was set to 320 ° C., and the core temperature of 90 ° C. for 1 second was finished with 130 g of hamburger and 8 minutes was completed with 70 g of hamburger and the core temperature of 90 ° C. was finished for 1 second. At this time, cooking worthy of sterilization effect + formation of the grilled surface by baking + edible was possible.

次に前記第1実施例の装置をホウレンソウのブランチングに適用した第5実施例について説明する。庫内温度を200℃に設定し、メッシュベルト1m当たり5kgのホウレンソウを2束程度積層させ、1分処理で青々として、シャキシャキ感のある食感を特徴とするブランチングホウレンソウが調理できた。また歩留まりが98.7%であった。 Next, a fifth embodiment in which the apparatus of the first embodiment is applied to spinach blanching will be described. The inside temperature was set to 200 ° C., about 2 bundles of 5 kg of spinach per 1 m 2 of the mesh belt were laminated, and blanching spinach characterized by a crisp texture with a crisp texture after 1 minute treatment could be cooked. The yield was 98.7%.

本発明によれば、加熱スピードが速くて処理効率が高く、安全性に問題がなく、個々の食品の解凍、加熱、殺菌、蒸煮、焼成、乾燥、ブランチングなどの調理等各種用途に最適な条件設定を容易に行なうことのできる加熱方法及び加熱装置を実現することができる。   According to the present invention, the heating speed is high, the processing efficiency is high, there is no safety problem, and it is most suitable for various uses such as thawing, heating, sterilization, steaming, baking, drying, and blanching of individual foods. It is possible to realize a heating method and a heating apparatus capable of easily setting conditions.

本発明装置の第1実施例の断面立面図である。1 is a sectional elevation view of a first embodiment of the device of the present invention. 前記第1実施例の断面平面図である。2 is a cross-sectional plan view of the first embodiment. FIG. 前記第1実施例の制御系の系統図である。It is a systematic diagram of the control system of the first embodiment. 前記第1実施例の制御装置のブロック線図である。It is a block diagram of the control apparatus of the said 1st Example. 本発明の第2実施例におけるテストピース移動雰囲気温度の測定結果を示す線図である。It is a diagram which shows the measurement result of the test piece movement atmosphere temperature in 2nd Example of this invention. 本発明の第2実施例におけるテストピース表面温度の測定結果を示すグラフである。It is a graph which shows the measurement result of the test piece surface temperature in 2nd Example of this invention. (a)及び(b)は、本発明の第3実施例における外観測定結果を示すグラフである。(A) And (b) is a graph which shows the external appearance measurement result in 3rd Example of this invention.

符号の説明Explanation of symbols

1 筐体
2 入口開口
3 出口開口
4 コンベアベルト
5 従動スプロケット
6 駆動スプロケット
7,8 ケーシング
9,28 駆動モータ
10 二次加熱機
11 高周波発生装置
12 一次蒸気管路
13,14 循環管路
15 上部ヘッダ
16 下部ヘッダ
17,18,19,20,21,22,23,24 ノズル管
25 基台
26 底板
27 循環ブロア
29 吸込口
30 チェーンベルト
31,35 温度センサ
40,41 流量調整弁
42 ラジエータ
43,44 冷却水循環管路
45 点検扉
46 キャスター
47 開閉弁付排水口
DESCRIPTION OF SYMBOLS 1 Case 2 Inlet opening 3 Outlet opening 4 Conveyor belt 5 Driven sprocket 6 Drive sprocket 7, 8 Casing 9, 28 Drive motor 10 Secondary heater 11 High frequency generator 12 Primary steam line 13, 14 Circulation line 15 Upper header 16 Lower header 17, 18, 19, 20, 21, 22, 23, 24 Nozzle pipe 25 Base 26 Bottom plate 27 Circulating blower 29 Suction port 30 Chain belt 31, 35 Temperature sensor 40, 41 Flow control valve 42 Radiator 43, 44 Cooling water circulation line 45 Inspection door 46 Caster 47 Drain outlet with on-off valve

Claims (7)

高耐熱性パネルで囲われた閉空間に、同閉空間を貫く高耐熱性のコンベアで食品を搬送させながら、連続的に加熱する装置において、他の加熱源で発生した一次水蒸気を誘電加熱又は誘導加熱によって150〜350℃に加熱し二次高温水蒸気を製造する二次加熱装置と、前記閉空間に分散配置され同閉空間に前記二次高温水蒸気を供給する複数のノズルと、同閉空間から排蒸気を排気する排気口と前記加熱装置とを接続する排蒸気循環路と、同排蒸気循環路に介設された高耐熱性ブロアと、前記二次加熱装置に一次水蒸気を供給する流路及び前記排蒸気循環路に設けられ、一次水蒸気の供給割合を調節可能にした弁機構とを備えたことを特徴とする食品加熱装置。   In a device that continuously heats food in a closed space surrounded by a high heat-resistant panel while transporting food on a high-heat-resistant conveyor that penetrates the closed space, the primary water vapor generated by another heating source is dielectrically heated or A secondary heating device for producing secondary high-temperature steam by heating to 150 to 350 ° C. by induction heating, a plurality of nozzles distributed in the closed space and supplying the secondary high-temperature steam to the closed space, and the closed space The exhaust steam circulation path connecting the exhaust device for exhausting the exhaust steam from the heating device, the high heat resistant blower interposed in the exhaust steam circulation channel, and the flow for supplying the primary steam to the secondary heating device A food heating apparatus comprising a valve mechanism and a valve mechanism provided in the exhaust steam circulation path and capable of adjusting a supply rate of primary steam. 前記コンベアの上下に複数のノズル管を分散配置し、前記閉空間の入口及び出口の上方に配置されたノズル管を食品の搬送方向と直角方向に配置したストレート型とするとともに、これらノズル管のノズル開口を真下に向け、前記ストレート型ノズル管以外はループ型とし、コンベアの上方に配置されたループ型ノズル管のノズル開口を前記閉空間の中央側に傾斜させ、下方に配置されたループ型ノズル管のノズル開口を真下に向けたことを特徴とする請求項1記載の食品加熱装置。   A plurality of nozzle tubes are arranged in a distributed manner above and below the conveyor, and the nozzle tubes arranged above the inlet and outlet of the closed space are arranged in a direction perpendicular to the direction of food conveyance, and the nozzle tubes The nozzle opening is directly below, the loop type other than the straight type nozzle pipe is a loop type, the nozzle type of the loop type nozzle pipe arranged above the conveyor is inclined toward the center side of the closed space, and the loop type arranged below 2. The food heating apparatus according to claim 1, wherein the nozzle opening of the nozzle tube is directed downward. 前記閉空間を形成する筐体の前記コンベアの長手方向に沿う側壁面に点検扉を設け、同筐体の底面を形成する底板を着脱可能とし、同底板に排水口を設け、同筐体内部を洗浄可能にしたことを特徴とする請求項1記載の食品加熱装置。   An inspection door is provided on a side wall surface of the casing that forms the closed space along the longitudinal direction of the conveyor, a bottom plate that forms the bottom surface of the casing is detachable, a drain outlet is provided in the bottom plate, and the inside of the casing The food heating apparatus according to claim 1, wherein the food can be washed. 前記加熱装置本体を収容した筐体の下部にキャスターを設け、同筐体を移動可能にしたことを特徴とする請求項1記載の食品加熱装置。   2. The food heating apparatus according to claim 1, wherein a caster is provided at a lower portion of a casing that houses the heating apparatus main body, and the casing is movable. 請求項1記載の食品加熱装置において、前記閉空間の温度を検出する温度センサによって閉空間の温度状況をモニタし、このデータ情報に基づいて前記ブロアの回転数を比例制御によって調節することにより、前記閉空間の温度を150〜350℃に制御するとともに、前記二次加熱装置の出口側水蒸気の温度を検出する温度センサにより出口側水蒸気温度をモニタし、このデータ情報に基づいて前記二次加熱装置の出力を比例制御によって調節することにより、同二次加熱装置の出口側水蒸気の温度を制御することを特徴とする食品加熱方法。   In the food heating apparatus according to claim 1, by monitoring the temperature state of the closed space by a temperature sensor that detects the temperature of the closed space, and adjusting the rotational speed of the blower by proportional control based on this data information, The temperature of the closed space is controlled to 150 to 350 ° C., and the outlet water vapor temperature is monitored by a temperature sensor that detects the temperature of the outlet water vapor of the secondary heating device, and the secondary heating is performed based on this data information. A food heating method, wherein the temperature of the outlet side water vapor of the secondary heating device is controlled by adjusting the output of the device by proportional control. 前記閉空間内で温度センサを前記コンベアで搬送される食品の近傍に設け、食品近傍の温度状況をモニタすることを特徴とする請求項4記載の食品加熱方法。   The food heating method according to claim 4, wherein a temperature sensor is provided in the vicinity of the food conveyed by the conveyor in the closed space, and the temperature condition in the vicinity of the food is monitored. 食品を蒸煮又は焼成するに際し、一次水蒸気の前記二次加熱装置への供給量及び前記閉空間の温度を調整することにより、前記閉空間の水蒸気の相対湿度を3〜6%RHに制御することを特徴とする請求項4記載の食品加熱方法。   When cooking or baking food, the relative humidity of water vapor in the closed space is controlled to 3 to 6% RH by adjusting the supply amount of primary water vapor to the secondary heating device and the temperature of the closed space. The food heating method according to claim 4.
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Cited By (10)

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JP2009201502A (en) * 2008-01-31 2009-09-10 Fuji Electric Systems Co Ltd Heat treatment apparatus using superheated steam
JP2011120487A (en) * 2009-12-08 2011-06-23 Taiyo Seisakusho Co Ltd Continuous heating method and continuous heating apparatus
JP2011200198A (en) * 2010-03-26 2011-10-13 Shinnetsu Kogyo Kk Method for baking food surface
CN105285664A (en) * 2015-11-23 2016-02-03 中国农业科学院农产品加工研究所 Traditional meat product integrated quantitative marinating apparatus
JP6010240B1 (en) * 2015-03-13 2016-10-19 ケレス株式会社 Heating / cooling integrated food processing system
CN107432664A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 A kind of efficient pressurization steam box equipment
CN107432665A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 A kind of transformation steam box equipment
CN107432671A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 A kind of sectional pressurization steam box equipment
CN107432670A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 The flexible pressurization steam box equipment of one kind assembling
JP2019177043A (en) * 2018-03-30 2019-10-17 株式会社中西製作所 Cooking apparatus

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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009201502A (en) * 2008-01-31 2009-09-10 Fuji Electric Systems Co Ltd Heat treatment apparatus using superheated steam
JP2011120487A (en) * 2009-12-08 2011-06-23 Taiyo Seisakusho Co Ltd Continuous heating method and continuous heating apparatus
JP2011200198A (en) * 2010-03-26 2011-10-13 Shinnetsu Kogyo Kk Method for baking food surface
US10561154B2 (en) 2015-03-13 2020-02-18 Cerecs Co., Ltd. Integrated heating and cooling food processing system
JP6010240B1 (en) * 2015-03-13 2016-10-19 ケレス株式会社 Heating / cooling integrated food processing system
JP2017055762A (en) * 2015-03-13 2017-03-23 ケレス株式会社 Integrated heating and cooling type food processing system
US11432558B2 (en) 2015-03-13 2022-09-06 Hakubai Co., Ltd. Integrated heating and cooling food processing system
CN105285664A (en) * 2015-11-23 2016-02-03 中国农业科学院农产品加工研究所 Traditional meat product integrated quantitative marinating apparatus
CN107432664A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 A kind of efficient pressurization steam box equipment
CN107432670A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 The flexible pressurization steam box equipment of one kind assembling
CN107432671A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 A kind of sectional pressurization steam box equipment
CN107432665A (en) * 2016-12-31 2017-12-05 广州普隆智能设备有限公司 A kind of transformation steam box equipment
JP2019177043A (en) * 2018-03-30 2019-10-17 株式会社中西製作所 Cooking apparatus
JP7163048B2 (en) 2018-03-30 2022-10-31 株式会社中西製作所 cooking device

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