JP2007061140A - Continuous steaming apparatus - Google Patents

Continuous steaming apparatus Download PDF

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Publication number
JP2007061140A
JP2007061140A JP2005247316A JP2005247316A JP2007061140A JP 2007061140 A JP2007061140 A JP 2007061140A JP 2005247316 A JP2005247316 A JP 2005247316A JP 2005247316 A JP2005247316 A JP 2005247316A JP 2007061140 A JP2007061140 A JP 2007061140A
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JP
Japan
Prior art keywords
steam
steaming
spiral structure
hollow
hollow spiral
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2005247316A
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Japanese (ja)
Inventor
Yoshio Nishida
淑男 西田
Kazuya Kobayakawa
和也 小早川
Takashi Kamine
崇 上根
Masashige Asano
正成 浅野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ASANO SHOKUHIN KK
KAMINE PRECISION MACHINERY
KAMINE SEIKI KOGYO KK
Aichi Prefecture
Original Assignee
ASANO SHOKUHIN KK
KAMINE PRECISION MACHINERY
KAMINE SEIKI KOGYO KK
Aichi Prefecture
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Publication date
Application filed by ASANO SHOKUHIN KK, KAMINE PRECISION MACHINERY, KAMINE SEIKI KOGYO KK, Aichi Prefecture filed Critical ASANO SHOKUHIN KK
Priority to JP2005247316A priority Critical patent/JP2007061140A/en
Publication of JP2007061140A publication Critical patent/JP2007061140A/en
Pending legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a continuous steaming apparatus that can supply steam evenly over a steamed object such as rice even with low vapor pressure, prevent blocking or uneven steaming, prevent dew condensation caused by temperature differences, sufficiently control temperature, and continuously and efficiently steam the steamed object. <P>SOLUTION: A hollow spiral structure 6 that can approximately quantity-deliver a steamed object 5 is rotatably supported in a rotatable manner at the bottom part 3 inside a tank 2 where a plurality of steam discharging openings 4 are provided. The hollow spiral structure 6 is provided with an exhaust pipe 7 which is extended outward from one side of the tank 2. The steamed object 5 put inside the tank 2 is supplied with steam from the steam discharging openings 4 while the hollow spiral structure 6 is rotating and the steamed object 5 is transferred to the exhaust pipe 7 side. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、穀類、雑穀類、豆類及び香辛料などの粉粒体の食品を、調理、殺菌あるいは
殺虫などの目的のために、蒸気による処理を行うための連続蒸煮装置に関する。
The present invention relates to a continuous steaming apparatus for treating steamed foods such as cereals, millet grains, beans, and spices for the purpose of cooking, sterilization, or insecticide.

食品を蒸煮により調理する際に、蒸気を通す構造のセイロなどの容器と、その下の蒸気
を発生させる鍋釜との組み合わせからなる蒸煮装置、所謂、蒸し器がある。この蒸し器は
、穀類、饅頭、点心、肉加工品などの蒸煮対象物をセイロに入れ、これらに蒸気を一定時
間送り続けて蒸煮するものである。したがって、この蒸し器は、蒸煮している状態での蒸
煮対象物の移動は無いから、バッチ式蒸煮装置と言える。
When cooking food by cooking, there is a so-called steamer, which is a steaming device comprising a combination of a container such as a steamer that allows steam to pass through and a pot pot that generates steam underneath. This steamer puts steamed objects such as cereals, buns, dim sum, and processed meat products into a cello, and steams them by continuously sending steam for a certain period of time. Therefore, this steamer can be said to be a batch-type steaming device because there is no movement of the steaming object in the steaming state.

上記したバッチ式蒸煮装置は、少量の蒸煮対象物を蒸煮するのには都合が良いが、多量
の蒸煮対象物を次々と蒸煮するのには効率的ではない。したがって、蒸煮対象物を連続し
て蒸煮することが出来る、下記のような連続蒸煮装置が知られている。
The above-described batch-type steaming apparatus is convenient for steaming a small amount of steaming object, but is not efficient for steaming a large amount of steaming object one after another. Therefore, the following continuous cooking apparatus which can cook a steaming target object continuously is known.

特開平7−327617号公報JP-A-7-327617 特開2002−85045号公報JP 2002-85045 A 特開2001−149223号公報JP 2001-149223 A 特許第3300906号Japanese Patent No. 3300906

この特許文献1に記載された連続蒸煮装置は、図8に示すように、タンクaの底部中央
にスクリューbが配設された排出樋cが設けられ、この排出樋cの端に排出口dが開けら
れ、更にスクリューb上方のタンクa内に複数の蒸気吹出開口eを有する蒸気管fが差し
込まれてなる。そして、タンクa内に投入された蒸煮対象物、例えば、洗米及び浸漬後の
米は、蒸気管fの複数の蒸気吹出開口eからの蒸気が当たることになり、スクリューbに
より排出樋c内を排出口dに向けて搬送される間に蒸煮されるものである。
As shown in FIG. 8, the continuous cooking apparatus described in Patent Document 1 is provided with a discharge bowl c in which a screw b is disposed at the bottom center of the tank a, and a discharge port d at the end of the discharge bowl c. And a steam pipe f having a plurality of steam outlets e is inserted into the tank a above the screw b. And the steaming target object thrown into the tank a, for example, the rice after washing and soaking, will be subjected to the steam from the plurality of steam outlets e of the steam pipe f, and the inside of the discharge pad c by the screw b. It is cooked while being conveyed toward the discharge port d.

また特許文献2に記載された連続蒸煮装置は、図9に示すように、機体g内にネットコ
ンベアhが配設され、このネットコンベアhの直下に蒸気供給室iがあり、このネットコ
ンベアh上に投入された洗米及び浸漬後の米は、蒸気供給室iからの蒸気が当たり、ネッ
トコンベアhが排出側に移動している間に蒸煮されるものである。
Moreover, as shown in FIG. 9, the continuous cooking apparatus described in Patent Document 2 includes a net conveyor h in the body g, and a steam supply chamber i immediately below the net conveyor h. The washed rice and the soaked rice introduced above are steamed while the steam from the steam supply chamber i hits and the net conveyor h moves to the discharge side.

また特許文献3に記載された連続蒸煮装置は、図10に示すように、下壁面jに蒸気吹
出開口eが設けられている蒸煮路kが傾斜状態に設けられ、この蒸煮路kの上端が供給口
mであり、下端が排出口dであって、更にこの排出口dに扉n及び切出具oが設けられて
なる。そして、供給口mから洗米及び浸漬後の米が供給されると、蒸煮路k内が満杯とな
り蒸気吹出開口eからの蒸気により蒸煮される。排出口dの扉nが開かれ切出具oにより
蒸煮後の米が切り出されると、後は自重により蒸煮路k内を通過する過程で順次蒸煮され
る。
Moreover, as shown in FIG. 10, the continuous cooking apparatus described in patent document 3 is provided with the cooking path k in which the steam blowing opening e is provided in the lower wall surface j in the inclined state, and the upper end of this cooking path k is It is the supply port m, the lower end is the discharge port d, and the discharge port d is further provided with a door n and a cutting tool o. And if the washing | cleaning rice and the rice after immersion are supplied from the supply port m, the inside of the steaming path k will become full and it will be cooked with the steam from the steam blowing opening e. When the door n of the discharge port d is opened and the cooked rice is cut out by the cutting tool o, the rice is subsequently cooked in the process of passing through the cooking path k by its own weight.

さらに特許文献4に記載された連続蒸煮装置は、図11に示すように、タンクaの底板
p及び側板qに蒸気吹出開口eを設け、且つタンクaの底部にスクリューbである定量フ
ィーダーを設けると共に排出管rをタンクaの側面から延出して設け、排出管rの出口s
側を上方に湾曲させ出口sの端面を水平面に対して15度乃至75度の傾斜を有するよう
にしたものである。そして、タンクa内に一定量の米を入れた状態で蒸気吹出開口eから
蒸気を吹き出すと共に、スクリューbを回転させているから、米を蒸煮しつつ排出管rの
出口s側に移動させ、排出管r内に蒸煮し終わった米を排出管rの湾曲効果により満管状
態にしてから、出口sより排出する。その際、出口sの端面が有する上記傾斜により、出
口sから連続的に排出している米を平面状にすり切り出来るので正確に計量することが可
能となる。
Furthermore, as shown in FIG. 11, the continuous cooking apparatus described in Patent Document 4 is provided with a steam blowing opening e in the bottom plate p and the side plate q of the tank a, and a metering feeder which is a screw b at the bottom of the tank a. And a discharge pipe r extending from the side surface of the tank a, and an outlet s of the discharge pipe r.
The side is curved upward and the end face of the outlet s has an inclination of 15 to 75 degrees with respect to the horizontal plane. And since steam is blown out from the steam blowout opening e in a state where a certain amount of rice is put in the tank a and the screw b is rotated, the rice is steamed and moved to the outlet s side of the discharge pipe r, The rice that has been cooked in the discharge pipe r is made full by the bending effect of the discharge pipe r and then discharged from the outlet s. At that time, because of the inclination of the end face of the outlet s, the rice continuously discharged from the outlet s can be ground into a flat shape, so that it can be accurately measured.

ところが、特許文献1に記載の連続蒸煮装置は、スクリューbにより排出樋c内を排出
口dに向けて蒸煮対象物の米を搬送する間に、スクリューbの上方に位置する蒸気管fの
蒸気吹出開口eからの蒸気により、米を蒸煮する点で効率的であるが、スクリューbの上
方の蒸気管fから蒸気を供給するから、蒸気の流れが一定方向であり、蒸気管fからの距
離の遠近により温度差が生じ、熱供給が不足して結露水が発生したり、蒸煮後の米の品質
にバラツキが生じ易い。更に、蒸煮膨張している米に万遍なく蒸気を行き渡らせるだけの
蒸気圧が必要となって、温度制御よりも蒸気圧制御を優先せざるをえないことになり、き
め細かい温度管理が不十分となるきらいがある。
However, in the continuous steaming device described in Patent Document 1, the steam in the steam pipe f located above the screw b is conveyed while the rice to be cooked is conveyed by the screw b toward the discharge port d through the discharge trough c. It is efficient in that rice is cooked by steam from the blowout opening e. However, since steam is supplied from the steam pipe f above the screw b, the steam flow is in a certain direction, and the distance from the steam pipe f. Due to the difference in temperature, there is a temperature difference, the heat supply is insufficient, and condensed water is generated, and the quality of the rice after cooking is likely to vary. In addition, steam pressure is required to spread steam uniformly over the steamed rice, and steam pressure control must be prioritized over temperature control, and fine temperature management is insufficient. There is a disagreement.

また、特許文献2に記載の連続蒸煮装置は、ネットコンベアh上に投入した蒸煮対象物
の米を、排出側に移動している間に蒸煮する点で効率的であるが、ネットコンベアh下の
蒸気供給室iよりネットコンベアh上の米に蒸気を供給するから、蒸気の流れが一定方向
であり、蒸気供給室iからの距離の遠近により温度差が生じ、文献1と同様に結露水が発
生したり、更に、ネットコンベアhは移動するがその上の米は動かないから、固定的な蒸
気の通り道が出来、蒸煮後の米の品質にバラツキが生じる。また、ネットコンベアh上の
蒸煮膨張している米間を吹き抜け、米に万遍なく蒸気を行き渡らせるだけの蒸気圧が必要
となって、特許文献1と同様に温度管理が不十分となるきらいがある。
Moreover, although the continuous cooking apparatus of patent document 2 is efficient at the point which cooks the rice of the cooking target thrown in on the net conveyor h while moving to the discharge side, Since steam is supplied from the steam supply chamber i to the rice on the net conveyor h, the flow of the steam is in a certain direction, and a temperature difference occurs depending on the distance from the steam supply chamber i. In addition, the net conveyor h moves, but the rice above it does not move, so a fixed steam path is created, and the quality of the cooked rice varies. In addition, steam pressure that blows through the steaming and expanding rice on the net conveyor h and spreads the steam evenly over the rice is necessary, and the temperature control is insufficient as in Patent Document 1. There is.

また、特許文献3に記載の連続蒸煮装置は、傾斜状態の蒸煮路k内で蒸煮対象物の米を
、自重により排出口d側に移動している間に蒸煮する点で効率的であるが、蒸煮路k下の
蒸気吹出開口eより蒸気を供給するから、蒸気の流れが一定方向であり、蒸気吹出開口e
からの距離の遠近により温度差が生じ、文献1と同様に結露水が発生したり、更に、文献
1と同様の理由で蒸気の通り道が出来やすく、蒸煮後の米の品質にバラツキが生じる。ま
た、蒸煮路k内の蒸煮膨張している米間を吹き抜け、米に万遍なく蒸気を行き渡らせるだ
けの蒸気圧が必要となって、特許文献1と同様に温度管理が不十分となるきらいがある。
Moreover, although the continuous cooking apparatus of patent document 3 is efficient in the point which cooks the rice of a steaming target object in the inclined cooking path k while moving to the discharge port d side by dead weight. Since steam is supplied from the steam outlet opening e below the steaming path k, the flow of steam is constant, and the steam outlet opening e
The temperature difference occurs depending on the distance from the water, and condensed water is generated as in the case of Reference 1, and further, the passage of steam is easily made for the same reason as in Reference 1, and the quality of the cooked rice varies. In addition, steam pressure that blows through the steam-expanding rice in the steaming path k and spreads the steam evenly over the rice is necessary, and the temperature control is insufficient as in Patent Document 1. There is.

また、特許文献4に記載の連続蒸煮装置は、スクリューbによりタンクa内を排出管r
に向けて蒸煮対象物の米を搬送する間に、タンクaの底板p及び側板qの蒸気吹出開口e
からの蒸気により、米を蒸煮する点で効率的であるが、タンクaの蒸気吹出開口eから蒸
気を供給するから、蒸気の流れがほぼ一定方向であり、蒸気吹出開口eからの距離の遠近
により温度差が生じ易く、必要以上に蒸気を供給することになり易い。更に、蒸煮膨張し
ている米に万遍なく蒸気を行き渡らせるだけの蒸気圧が必要となって、温度制御よりも蒸
気圧制御を優先することになり、きめ細かい温度管理が不十分となるきらいがある。
Moreover, the continuous cooking apparatus described in Patent Document 4 uses a screw b to evacuate a tank a with a discharge pipe r.
While conveying the rice to be steamed toward the steam outlet opening e of the bottom plate p and the side plate q of the tank a
Is efficient in steaming rice with steam from the steam, but since steam is supplied from the steam outlet opening e of the tank a, the flow of steam is almost constant, and the distance from the steam outlet e Therefore, a temperature difference is likely to occur, and it is easy to supply steam more than necessary. In addition, steam pressure is required to spread the steam evenly over the steaming rice, giving priority to steam pressure control over temperature control, and fine temperature management is not sufficient. is there.

そこで、本発明の目的は、上記先行技術の問題点を解消し、蒸気圧を高くしなくても、
蒸煮対象物に蒸気を万遍なく供給できて、蒸煮対象物のブロッキングや蒸煮むらを防ぎ、
加えて温度差による結露水を防いで、しかもきめ細かい温度管理も充分に出来て、蒸煮対
象物を連続して効率よく蒸煮することが出来る連続蒸煮装置を提供することにある。
Therefore, the object of the present invention is to solve the above-mentioned problems of the prior art, without increasing the vapor pressure,
Steam can be supplied evenly to the steaming object, preventing the steaming object from blocking or steaming,
In addition, an object of the present invention is to provide a continuous cooking apparatus that prevents condensation water due to a temperature difference, can also perform fine temperature control sufficiently, and can continuously and efficiently cook an object to be cooked.

本発明は、上記目的を達成するために提案されたものであって、下記の構成からなるこ
とを特徴とするものである。
すなわち、本発明によれば、タンク内の底部に、複数の蒸気吹出開口を有すると共に蒸
煮対象物をほぼ定量搬送可能な中空スパイラル構造体を回転自在に軸支し、且つ該中空ス
パイラル構造体の排出管を前記タンクの側面から延出して設けてなり、前記タンク内に投
入された蒸煮対象物に、前記中空スパイラル構造体を回転させた状態で、前記蒸気吹出開
口からの蒸気を供給すると共に、蒸煮対象物を前記排出管側に搬送するようにしたことを
特徴とする連続蒸煮装置が提供される。
The present invention has been proposed in order to achieve the above object, and is characterized by having the following configuration.
That is, according to the present invention, a hollow spiral structure having a plurality of steam blowing openings at the bottom of the tank and capable of substantially quantitatively transporting a steaming object is rotatably supported, and the hollow spiral structure is A discharge pipe is provided so as to extend from the side surface of the tank, and steam from the steam blowout opening is supplied to a steaming target charged in the tank while the hollow spiral structure is rotated. There is provided a continuous cooking apparatus characterized in that a steaming object is conveyed to the discharge pipe side.

また、本発明によれば、前記タンクの底板及び側板の少なくと底板に、蒸気排出口を複
数設けて、蒸煮対象物を蒸煮処理した後の過剰な蒸気を前記タンク内から外部に排除する
ことを特徴とする上記連続蒸煮装置が提供される。
Further, according to the present invention, at least a bottom plate and a side plate of the tank are provided with a plurality of steam outlets, and excess steam after the steaming object is steamed is excluded from the tank to the outside. The above-mentioned continuous steaming device is provided.

また、本発明によれば、前記中空スパイラル構造体は中空軸と羽根とからなり、前記中
空軸に前記蒸気吹出開口を複数開けてなることを特徴とする上記連続蒸煮装置が提供され
る。
In addition, according to the present invention, there is provided the continuous steaming device, wherein the hollow spiral structure includes a hollow shaft and a blade, and a plurality of the steam blowing openings are formed in the hollow shaft.

また、本発明によれば、前記羽根は中空であり、該中空羽根に前記蒸気吹出開口を複数
開けてなることを特徴とする上記連続蒸煮装置が提供される。
Moreover, according to this invention, the said blade | wing is hollow, The said steaming opening is opened in this hollow blade | wing, The said continuous cooking apparatus characterized by the above-mentioned is provided.

また、本発明によれば、前記中空スパイラル構造体の前記羽根の外径(D1)と前記中
空軸の外径(D2)との比率(D1/D2)は、1.1乃至15としたことを特徴とする
上記連続蒸煮装置が提供される。
Further, according to the present invention, the ratio (D1 / D2) between the outer diameter (D1) of the blade of the hollow spiral structure and the outer diameter (D2) of the hollow shaft is 1.1 to 15. The above-mentioned continuous steaming device is provided.

また、本発明によれば、前記羽根の外径(D1)と前記中空スパイラル構造体の実効長
さ(L)との比率(D1/L)は、0.1乃至10としたことを特徴とする上記連続蒸煮
装置が提供される。
According to the present invention, the ratio (D1 / L) between the outer diameter (D1) of the blade and the effective length (L) of the hollow spiral structure is 0.1 to 10. The above-mentioned continuous cooking apparatus is provided.

また、本発明によれば、前記排出管はその出口側を上方に湾曲させてなり、前記排出管
の出口の端面中心部は、前記中空スパイラル構造体の軸心よりも、前記羽根の外径(D1
)の0.1乃至5倍垂直方向に高く位置するようにしたことを特徴とする上記連続蒸煮装
置が提供される。
Further, according to the present invention, the outlet pipe has its outlet side curved upward, and the center of the end face of the outlet of the outlet pipe has an outer diameter of the vane rather than the axial center of the hollow spiral structure. (D1
The above-mentioned continuous steaming device is provided which is positioned 0.1 to 5 times higher in the vertical direction.

また、本発明によれば、前記排出管は、前記中空スパイラル構造体の前記羽根の外径(
D1)に対して1乃至50mmのクリアランスを有し、且つ前記中空スパイラル構造体の
実効長さ(L)の0.01乃至2.0倍の長さを有することを特徴とする上記連続蒸煮装
置が提供される。
According to the present invention, the discharge pipe has an outer diameter of the blade of the hollow spiral structure (
D1) has a clearance of 1 to 50 mm and has a length that is 0.01 to 2.0 times the effective length (L) of the hollow spiral structure. Is provided.

また、本発明によれば、蒸煮対象物の蒸煮温度は、前記中空スパイラル構造体に供給す
る蒸気の温度を変えることにより、制御するようにしたことを特徴とする上記連続蒸煮装
置が提供される。
In addition, according to the present invention, there is provided the above-described continuous steaming device, wherein the steaming temperature of the steaming object is controlled by changing the temperature of steam supplied to the hollow spiral structure. .

本発明の連続蒸煮装置は、タンク内に蒸煮対象物を投入した状態で、中空スパイラル構
造体に蒸気を供給すると共に回転させると、その蒸気吹出開口も回転しながら蒸気を蒸煮
対象物に供給すると共に蒸煮対象物を排出管側に搬送し、その搬送の間に蒸煮対象物を蒸
煮するものであるため、蒸気吹出開口及び蒸煮対象物自体が絶えず移動しているから、蒸
気圧を高くしなくても、蒸煮対象物に蒸気を万遍なく供給できて、蒸煮対象物のブロッキ
ングや蒸煮むらを防ぎ、加えて温度差による結露水を防ぎ、しかも蒸気圧制御を主体にし
なくても良い分、きめ細かい温度管理も充分に出来て、蒸煮対象物を連続して効率良く蒸
煮することが出来る効果を得ることができる。
The continuous steaming apparatus of the present invention supplies steam to the steaming object while rotating the steam blowing opening when the steam is supplied to the hollow spiral structure and rotated while the steaming object is put in the tank. Since the steaming object is transported to the discharge pipe side and the steaming object is steamed during the transport, the steam outlet and the steaming object itself are constantly moving, so the steam pressure is not increased. However, steam can be uniformly supplied to the object to be cooked, blocking the steaming object and uneven cooking, in addition to preventing dew condensation due to temperature differences, and without having to focus on steam pressure control, Fine temperature control can be sufficiently performed, and an effect of continuously and efficiently steaming an object to be steamed can be obtained.

また、本発明の連続蒸煮装置において、中空スパイラル構造体の蒸気吹出開口から吹き
出た蒸気は蒸煮対象物に供給され蒸煮した後、タンクの底板及び側板の複数の蒸気排出口
からタンク外に排除される様にした場合は、上記効果に加えて、蒸煮対象物を蒸煮する場
所を蒸気吹出開口から蒸気排出口に至る中空スパイラル構造体の周辺部にすることが出来
て、蒸気供給、蒸煮及び搬送を一体化出来る効果が得られる。
Further, in the continuous cooking apparatus of the present invention, the steam blown out from the steam outlet opening of the hollow spiral structure is supplied to the subject to be cooked and then removed from the tank through a plurality of steam outlets on the bottom plate and side plate of the tank. In this case, in addition to the above effect, the steaming object can be steamed to the periphery of the hollow spiral structure from the steam outlet to the steam outlet. The effect that can be integrated is obtained.

また、本発明の連続蒸煮装置において、中空スパイラル構造体の中空軸に蒸気源を接続
してあれば、中空軸の蒸気吹出開口から蒸気を蒸煮対象物に供給することにより蒸煮でき
る。それによって、上記効果に加えて、蒸気供給機構を簡易にできる効果が得られる。
Moreover, in the continuous cooking apparatus of this invention, if a steam source is connected to the hollow shaft of a hollow spiral structure body, it can be cooked by supplying steam to a steaming target object from the steam blowing opening of a hollow shaft. Thereby, in addition to the above effects, an effect of simplifying the steam supply mechanism can be obtained.

また、本発明の連続蒸煮装置において、中空スパイラル構造体の中空軸の蒸気吹出開口
に加えて、中空羽根の蒸気吹出開口からも蒸気を蒸煮対象物に供給するようにした場合は
、上記効果に加えて、中空羽根の蒸気吹出開口からも蒸気が供給され、その分蒸煮対象物
をより効率良く蒸煮することができる。
In addition, in the continuous cooking apparatus of the present invention, in addition to the steam outlet opening of the hollow shaft of the hollow spiral structure, when steam is supplied from the steam outlet opening of the hollow blade to the steaming object, the above effect is achieved. In addition, steam is also supplied from the steam outlet opening of the hollow blade, and the steaming object can be steamed more efficiently.

また、本発明の連続蒸煮装置において、羽根の外径と中空軸の外径との比率を特定化し
たスパイラル構造体とすることにより、タンク内の蒸煮対象物を排出管の出口側に搬送す
ることができるため、上記効果に加えて、蒸煮後の蒸煮物を効率よくスムーズに搬送でき
る効果がある。
Moreover, in the continuous steaming apparatus of the present invention, the steaming object in the tank is conveyed to the outlet side of the discharge pipe by using a spiral structure in which the ratio between the outer diameter of the blade and the outer diameter of the hollow shaft is specified. Therefore, in addition to the above-described effects, there is an effect that the steamed food after cooking can be efficiently and smoothly conveyed.

また、本発明の連続蒸煮装置において、羽根の外径と中空スパイラル構造体の実効長さ
との比率を特定化したスパイラル構造体とすることにより、タンク内の蒸煮対象物を排出
管の出口側に搬送することができるため、上記効果に加えて、蒸煮後の蒸煮物を効率よく
スムーズに搬送できる効果がある。
Moreover, in the continuous steaming apparatus of the present invention, the steaming object in the tank is placed on the outlet side of the discharge pipe by using a spiral structure in which the ratio between the outer diameter of the blade and the effective length of the hollow spiral structure is specified. Since it can convey, in addition to the said effect, there exists an effect which can convey the steamed material after cooking efficiently and smoothly.

また、本発明の連続蒸煮装置において、蒸煮後の蒸煮物を、上方湾曲の排出管の出口近
傍で満管状態となってから出口より排出し、その際、出口の端面中心部が中空スパイラル
構造体の軸心よりも垂直方向に高く位置することにより、出口端面にある蒸煮物に凹凸が
生じにくくなるため、上記効果に加えて、蒸煮した後の蒸煮物を正確に計量出来る効果が
ある。
Moreover, in the continuous cooking apparatus of the present invention, the steamed product after cooking is discharged from the outlet after becoming full in the vicinity of the outlet of the upwardly curved discharge pipe, and at that time, the center part of the end face of the outlet is a hollow spiral structure By being positioned higher in the vertical direction than the axis of the body, it becomes difficult for irregularities to occur in the steamed food at the outlet end face, and in addition to the above effects, there is an effect of accurately measuring the steamed food after cooking.

また、本発明の連続蒸煮装置において、形状の羽根及び中空軸を特定化した中空スパイ
ラル構造体とすることにより、蒸煮後の蒸煮物を排出管内を通過させ得ることができるた
め、上記効果に加えて、蒸煮後の蒸煮物をスムーズに排出管中を通過させ得ることが出来
るという効果がある。
In addition, in the continuous steaming apparatus of the present invention, the steamed product after steaming can be passed through the discharge pipe by specifying the hollow blade and the hollow shaft of the shape, so that in addition to the above effects Thus, the steamed product after cooking can be smoothly passed through the discharge pipe.

また、本発明の連続蒸煮装置において、蒸煮対象物の最適な蒸煮温度に合わせて蒸気の
温度を設定し、その設定温度の蒸気を中空スパイラル構造体に供給して、蒸煮対象物を蒸
煮するようにすれば、上記効果に加えて、蒸煮対象物に最適な温度の蒸気を供給すること
で、良質な蒸煮物を得ることが出来、且つ効率よく蒸煮出来る効果がある。
Further, in the continuous cooking apparatus of the present invention, the steam temperature is set in accordance with the optimum steaming temperature of the steaming object, and steam at the set temperature is supplied to the hollow spiral structure so that the steaming object is steamed. If it makes it, in addition to the said effect, there exists an effect which can be cooked efficiently by being able to obtain a good-quality steamed food by supplying the steam of the optimal temperature to a steaming target object.

以下に、図面を参照して本発明を実施するための最良の形態を説明する。   The best mode for carrying out the present invention will be described below with reference to the drawings.

図1は本発明の好ましい実施の形態を示す連続蒸煮装置の正面図、図2は本発明の実施
の形態を示す連続蒸煮装置の平面図、図3は本発明の実施の形態を示す連続蒸煮装置の側
面図である。図において、1は連続蒸煮装置を示し、この連続蒸煮装置1は、タンク2内
の底部3に、複数の蒸気吹出開口4を有すると共に蒸煮対象物5をほぼ定量搬送可能な中
空スパイラル構造体6を回転自在に軸支し、且つこの中空スパイラル構造体6の排出管7
をタンク2の側面から延出して設けてなり、前記タンク2内に投入された蒸煮対象物5に
中空スパイラル構造体6を回転させた状態で蒸気吹出開口4からの蒸気を供給すると共に
、蒸煮対象物5を排出管7側に搬送するようにしたものである。
FIG. 1 is a front view of a continuous cooking apparatus showing a preferred embodiment of the present invention, FIG. 2 is a plan view of the continuous cooking apparatus showing the embodiment of the present invention, and FIG. 3 is a continuous cooking illustrating the embodiment of the present invention. It is a side view of an apparatus. In the figure, reference numeral 1 denotes a continuous cooking apparatus. The continuous cooking apparatus 1 has a hollow spiral structure 6 having a plurality of steam blowing openings 4 at the bottom 3 in a tank 2 and capable of conveying a steamed object 5 almost quantitatively. And a discharge pipe 7 of the hollow spiral structure 6.
Is provided to extend from the side surface of the tank 2, and steam is supplied from the steam outlet opening 4 while the hollow spiral structure 6 is rotated to the steaming object 5 put in the tank 2, and steaming is performed. The object 5 is conveyed to the discharge pipe 7 side.

前記タンク2は、上部開口が四角形をなし底部3がV字状をなしている。このタンク2
の上部開口には、蒸煮対象物5を投入するシュート等を取り付けるためのフランジ10が
形成されている。また、タンク2のV字状の底部3の外側は、板11で覆われて蒸気排出
室12が形成され、この蒸気排出室12は蒸気排出管13に接続されて、外部に蒸気が排
出されるようになっている。このタンク2の底板14及び側板15は、図4、5に示すよ
うに、多孔板になっていて、蒸煮対象物5が通過しない程度の径を有する蒸気排出口16
が無数に穿設され、タンク2内と蒸気排出室12内とは蒸気の流通が自在である。蒸気供
給は、蒸気供給源(図示せず)がタンク下の蒸気ヘッダー17につながり、この蒸気ヘッ
ダー17からパイプ17aを経て、前記中空スパイラル構造体6に接続することで、行な
われる。
The tank 2 has a rectangular upper opening and a V-shaped bottom 3. This tank 2
A flange 10 for attaching a chute or the like for charging the steaming object 5 is formed in the upper opening of the. Further, the outside of the V-shaped bottom 3 of the tank 2 is covered with a plate 11 to form a steam discharge chamber 12, which is connected to a steam discharge pipe 13, and steam is discharged to the outside. It has become so. As shown in FIGS. 4 and 5, the bottom plate 14 and the side plate 15 of the tank 2 are perforated plates and have a diameter that does not allow the steaming object 5 to pass therethrough.
Are infinitely drilled, and steam can freely flow between the tank 2 and the steam discharge chamber 12. Steam supply is performed by connecting a steam supply source (not shown) to the steam header 17 under the tank and connecting the steam header 17 to the hollow spiral structure 6 through a pipe 17a.

また、蒸気供給は、中空スパイラル構造体6の上方に配備した蒸気供給パイプ18から
も可能にし、蒸煮対象物5のプレ蒸煮出来るようにしている。すなわち、蒸気ヘッダー1
7から調整弁19及びパイプ17aを経て、中空スパイラル構造体6と同様の蒸気吹出開
口4を複数穿設している蒸気供給パイプ18に接続している。したがって、蒸煮対象物5
の種類によりプレ蒸煮が必要である場合、調整弁19により蒸気供給量を調整してプレ蒸
煮も可能としている。なお、図1中、8は蒸煮対象物5の蒸煮状態を監視出来る覗き窓で
あり、図1、3中、9は蒸気ヘッダー17のドレーン弁である。
Further, the steam can be supplied from the steam supply pipe 18 disposed above the hollow spiral structure 6 so that the steaming object 5 can be pre-steamed. That is, steam header 1
7 is connected to a steam supply pipe 18 through which a plurality of steam blowout openings 4 similar to those of the hollow spiral structure 6 are formed, through a regulating valve 19 and a pipe 17a. Therefore, steamed object 5
When pre-cooking is necessary depending on the type of the steam, the steam supply amount is adjusted by the regulating valve 19 to enable pre-cooking. In FIG. 1, reference numeral 8 denotes a viewing window that can monitor the cooking state of the cooking object 5, and in FIGS. 1 and 3, 9 denotes a drain valve of the steam header 17.

前記中空スパイラル構造体6は、図6に示すような中空軸20と羽根21とからなるス
クリュータイプであり、回転することにより蒸煮対象物5を搬送出来、中空軸20に蒸煮
対象物5が通過しない程度の径を有する上記の蒸気吹出開口4を複数穿設してなるもので
ある。この中空スパイラル構造体6は、その回転数により蒸煮対象物5の搬送量を可変出
来、モータ(図示せず)により0.5乃至360rpmの範囲で無段変速できるものが選
択される。更に、この中空スパイラル構造体6の回転数は、好ましくは1乃至120rp
mの範囲であり、より好ましくは2乃至60rpmの範囲である。これによって、この中
空スパイラル構造体6の中空軸20に蒸気発生源を接続しておけば、蒸煮対象物5を搬送
しながら蒸気吹出開口4から蒸気を蒸煮対象物5に供給できて、排出管7側に搬送するま
での間に蒸煮対象物5を蒸煮することができる。
The hollow spiral structure 6 is a screw type including a hollow shaft 20 and blades 21 as shown in FIG. 6, and can rotate the steaming object 5 by rotating, and the steaming object 5 passes through the hollow shaft 20. A plurality of the above-described steam blowout openings 4 having a diameter not to be formed are formed. The hollow spiral structure 6 is selected so that the amount of the steaming object 5 can be varied depending on the number of rotations thereof and can be continuously variable within a range of 0.5 to 360 rpm by a motor (not shown). Further, the rotational speed of the hollow spiral structure 6 is preferably 1 to 120 rp.
m, more preferably 2 to 60 rpm. Accordingly, if a steam generation source is connected to the hollow shaft 20 of the hollow spiral structure 6, steam can be supplied to the steaming object 5 from the steam blowout opening 4 while the steaming object 5 is conveyed, and the discharge pipe The steaming object 5 can be steamed until it is conveyed to the 7 side.

また、図7に示す中空スパイラル構造体6aは羽根も中空とし、この中空羽根21aに
も蒸気吹出開口4を複数穿設してなる。したがって、中空軸20の蒸気吹出開口4に加え
て、中空羽根21aの蒸気吹出開口4からも蒸気が供給出来て、その分蒸煮対象物5をよ
り効率良く蒸煮することができる。なお、図7の中空スパイラル構造体6aは、中空軸2
0及び中空羽根21aの双方に蒸気吹出開口4を複数穿設してあるが、中空軸20に蒸気
吹出開口4を穿設せず、中空羽根21aのみに蒸気吹出開口4を複数穿設したものでも差
し支えない。
Further, the hollow spiral structure 6a shown in FIG. 7 has a hollow blade, and the hollow blade 21a is provided with a plurality of steam blowing openings 4. Therefore, in addition to the steam blowing opening 4 of the hollow shaft 20, steam can be supplied from the steam blowing opening 4 of the hollow blade 21a, and the steaming target object 5 can be steamed more efficiently. Note that the hollow spiral structure 6a in FIG.
A plurality of steam blowout openings 4 are formed in both the zero and hollow blades 21a, but a plurality of steam blowout openings 4 are formed only in the hollow blades 21a without forming the steam blowout openings 4 in the hollow shaft 20. But it doesn't matter.

また、前記中空スパイラル構造体6及び6aは、図6及び7に示すように、前記羽根2
1及び中空羽根21aの外径(D1)と、前記中空軸20及び20の外径(D2)との比
率(D1/D2)を1.1乃至15とする。この範囲の比率(D1/D2)であると、タ
ンク2内の蒸煮対象物5を排出管7の出口側にスムーズに搬送しつつ効率よく蒸煮するこ
とが出来る。
Further, the hollow spiral structures 6 and 6a are arranged on the blade 2 as shown in FIGS.
The ratio (D1 / D2) between the outer diameter (D1) of the first and hollow blades 21a and the outer diameter (D2) of the hollow shafts 20 and 20 is 1.1 to 15. When the ratio is within this range (D1 / D2), the steaming object 5 in the tank 2 can be efficiently steamed while being smoothly transported to the outlet side of the discharge pipe 7.

また、前記中空スパイラル構造体6及び6aは、図6及び7に示すように、前記羽根2
1及び中空羽根21aの外径(D1)と、中空スパイラル構造体6及び6aの実効長さ(
L)との比率(D1/L)を0.1乃至10とする。この範囲の比率(D1/L)である
と、タンク2内の蒸煮対象物5を排出管7の出口側にスムーズに搬送しつつ効率よく蒸煮
することが出来る。
Further, the hollow spiral structures 6 and 6a are arranged on the blade 2 as shown in FIGS.
1 and the outer diameter (D1) of the hollow blade 21a and the effective length of the hollow spiral structures 6 and 6a (
L) is set to 0.1 to 10 (D1 / L). When the ratio is within this range (D1 / L), the steaming object 5 in the tank 2 can be efficiently steamed while being smoothly transported to the outlet side of the discharge pipe 7.

また、前記排出管7は、その出口30側を上方に湾曲させた曲管31と、この曲管31
とタンク2の側面との間に介在する直管32とからなる。この曲管31の出口30の端面
30aの中心部が、中空スパイラル構造体6及び6aの中空軸20の軸心20aよりも、
前記羽根21及び中空羽根21aの外径(D1)の0.1乃至5倍垂直方向に高く位置し
ている。更に、この排出管7の曲管31及び直管32は、共に中空スパイラル構造体6及
び6aの前記羽根21及び中空羽根21aの外径(D1)に対して1乃至50mmのクリ
アランスを有し、且つ中空スパイラル構造体6及び6aの実効長さ(L)の0.01乃至
2.0倍の長さを有する。
The discharge pipe 7 includes a curved pipe 31 whose outlet 30 is bent upward, and the curved pipe 31.
And a straight pipe 32 interposed between the side surface of the tank 2. The central portion of the end face 30a of the outlet 30 of the curved pipe 31 is more than the axial center 20a of the hollow shaft 20 of the hollow spiral structures 6 and 6a.
The blades 21 and the hollow blades 21a are higher in the vertical direction by 0.1 to 5 times the outer diameter (D1). Further, the curved pipe 31 and the straight pipe 32 of the discharge pipe 7 both have a clearance of 1 to 50 mm with respect to the outer diameter (D1) of the blade 21 and the hollow blade 21a of the hollow spiral structures 6 and 6a. In addition, the hollow spiral structures 6 and 6a have a length 0.01 to 2.0 times the effective length (L).

前記排出管7が中空スパイラル構造体6及び6aとの関係において、上記したクリアラ
ンス及び長さを有することにより、蒸煮後の蒸煮物5aをスムーズに排出管7中を通過さ
せ得る。次に、排出管7中を通過して曲管31の出口30の端面30aに到達した蒸煮物
5aは、出口30近傍で満管状態となってから出口30より排出し、その際、出口30の
端面30aの中心部が中空軸20の軸心20aよりも垂直方向に充分高く位置しているか
ら、出口30の端面30aにある蒸煮物5aに凹凸が生じにくい状態となっている。この
ため、上部から切出板などで出口30の端面30aに沿い蒸煮後の蒸煮物5aをすり切り
すれば、蒸煮物5aに凹凸が生じないから正確に計量することが出来る。
When the discharge pipe 7 has the above-described clearance and length in relation to the hollow spiral structures 6 and 6a, the steamed product 5a after cooking can be smoothly passed through the discharge pipe 7. Next, the steamed product 5a that has passed through the discharge pipe 7 and has reached the end face 30a of the outlet 30 of the curved pipe 31 is discharged from the outlet 30 after becoming full in the vicinity of the outlet 30. Since the center part of the end face 30a is positioned sufficiently higher than the axis 20a of the hollow shaft 20 in the vertical direction, the steamed product 5a on the end face 30a of the outlet 30 is not easily uneven. For this reason, if the steamed material 5a after cooking is cut along the end face 30a of the outlet 30 with a cutting plate or the like from the upper part, the steamed material 5a is not uneven, so that it can be accurately measured.

翻って鑑みると、この連続蒸煮装置1では、中空スパイラル構造体6あるいは6aが蒸
気供給機能と搬送機能とを兼ね備え、タンク2内の底部3にある蒸煮対象物5に対し蒸気
を供給する蒸気吹出開口4自体が移動し、且つ蒸煮される蒸煮対象物5自体も羽根21及
び中空羽根21aにより絶えずかき回され移動している。このため、蒸煮対象物5のブロ
ッキングや蒸煮むらが生じる虞がなく、従来例のように蒸気圧を必要以上に高くしなくて
も、蒸煮対象物5に蒸気を万遍なく供給できる。よって、蒸煮を目的とする蒸気供給にお
いて、その実、蒸気圧制御を主体とせざるを得なかった点が解消され、供給蒸気の温度を
制御して、蒸煮対象物5ごとに最適蒸煮温度で蒸煮することが可能となった。
In retrospect, in this continuous steaming device 1, the hollow spiral structure 6 or 6a has both a steam supply function and a transport function, and steam is supplied to the steaming object 5 at the bottom 3 in the tank 2. The opening 4 itself is moved, and the steamed object 5 itself to be cooked is constantly stirred and moved by the blades 21 and the hollow blades 21a. For this reason, there is no possibility that the steaming object 5 may be blocked or unevenly steamed, and steam can be uniformly supplied to the steaming object 5 without increasing the steam pressure more than necessary as in the conventional example. Therefore, in the steam supply for the purpose of steaming, the fact that the fact that the steam pressure control has been the main subject has been solved, the temperature of the supplied steam is controlled, and steaming is performed at the optimum steaming temperature for each steaming object 5. It became possible.

したがって、蒸煮対象物5の蒸煮温度は、前記中空スパイラル構造体6あるいは6aに
蒸気発生源から供給する蒸気の温度を変えることにより制御する。すなわち、蒸煮対象物
5の最適な蒸煮温度に合わせて蒸気の温度を設定し、その設定温度の蒸気を中空スパイラ
ル構造体6あるいは6aを経由して蒸煮対象物5に供給し蒸煮することで、良質な蒸煮物
5aを得ることが出来、且つ効率良い蒸煮が出来る。この供給蒸気の温度制御は、特に限
定はないが、例示すれば、定圧膨張による100℃以下の飽和蒸気を生成して、この飽和
蒸気を中空スパイラル構造体6あるいは6aに供給し、更にこれから蒸煮対象物5に供給
し蒸煮したり、また、ロータリーバルブ式圧力制御方式であったり、また、オン−オフ式
圧力制御方式であったり、また、高圧蒸気発生器方式であったり、更に、蒸気排出室12
からの蒸気の抜き取り量を加減する方式であったりして、あるいは上記の組み合わせによ
る方式であったりする。そして、これら公知の蒸気の温度制御方式のいずれかを選択し、
採用する。
Therefore, the cooking temperature of the cooking object 5 is controlled by changing the temperature of the steam supplied from the steam generating source to the hollow spiral structure 6 or 6a. That is, by setting the steam temperature in accordance with the optimum steaming temperature of the steaming object 5, supplying steam to the steaming object 5 via the hollow spiral structure 6 or 6a and steaming, A high-quality steamed product 5a can be obtained, and efficient steaming can be performed. The temperature control of the supply steam is not particularly limited. For example, saturated steam having a temperature of 100 ° C. or less is generated by constant pressure expansion, and the saturated steam is supplied to the hollow spiral structure 6 or 6a. It is supplied to the object 5 and cooked, or it is a rotary valve pressure control system, an on-off pressure control system, a high pressure steam generator system, and steam discharge. Chamber 12
It may be a method for adjusting the amount of steam extracted from the steam, or a method based on the above combination. And select one of these known steam temperature control methods,
adopt.

次に、上記構成になる連続蒸煮装置1により蒸煮対象物である米5を蒸煮する場合につ
いて述べる。
まず、洗米及び浸漬して水切りした米5をタンク2内に適量投入する。米5の最適蒸煮
温度を設定し、蒸気発生源からの蒸気温度を採用した温度制御方式により制御して、最適
蒸煮温度の蒸気を中空スパイラル構造体6あるいは6aに供給する。次に、中空スパイラ
ル構造体6あるいは6aを0.5乃至360rpmの範囲内で設定した回転数、例えば、
10rpmで回転させて、中空スパイラル構造体6あるいは6aの中空軸20あるいは中
空軸20及び中空羽根21aの回転中の蒸気吹出開口4から蒸気を米5に供給する。その
際、米5は、上記と同じく回転中の羽根21及び中空羽根21aにより揺動しつつ、排出
管7の出口側に向けて搬送している。
Next, the case where the rice 5 which is a cooking object is cooked with the continuous cooking apparatus 1 which becomes the said structure is described.
First, a suitable amount of washed rice and soaked and drained rice 5 is put into the tank 2. The optimum cooking temperature of the rice 5 is set and controlled by a temperature control system employing the steam temperature from the steam generation source, and steam at the optimum cooking temperature is supplied to the hollow spiral structure 6 or 6a. Next, the rotational speed at which the hollow spiral structure 6 or 6a is set within a range of 0.5 to 360 rpm, for example,
By rotating at 10 rpm, steam is supplied to the rice 5 from the rotating shaft 4 of the hollow spiral structure 6 or 6a or the steam blowing opening 4 during rotation of the hollow shaft 20 and the hollow blade 21a. At that time, the rice 5 is conveyed toward the outlet side of the discharge pipe 7 while being swung by the rotating blade 21 and the hollow blade 21a as described above.

したがって、米5に固定的な蒸気の通り道が出来たり、米5がブロッキングしたりする
ことがなく、更に、タンク2の底部3に無数の蒸気排出口16があるから、蒸気吹出開口
4から供給した蒸気は直ちに米5に供給され蒸煮し、更に、蒸煮を終えた蒸気は直ちに蒸
気排出口16を通り一旦蒸気排出室12内に入り、外部に排出する。なお、米5のプレ蒸
煮が必要である場合は、調整弁19を開き供給量を調整して、蒸気供給パイプ18の蒸気
吹出開口18aから蒸気を投入直後の米5に供給することになる。
Accordingly, there is no fixed steam passage in the rice 5 or the rice 5 is blocked, and there are innumerable steam outlets 16 in the bottom 3 of the tank 2, so that the rice is supplied from the steam outlet 4. The steam is immediately supplied to the rice 5 and cooked, and the steam that has been cooked immediately passes through the steam discharge port 16 and once enters the steam discharge chamber 12 and is discharged outside. When pre-cooking of the rice 5 is necessary, the supply valve is adjusted by opening the regulating valve 19 and the steam is supplied to the rice 5 just after being introduced from the steam outlet opening 18a of the steam supply pipe 18.

一方、米5は、タンク2内に投入された後、回転中の羽根21及び中空羽根21aによ
り、排出管7の出口30から排出されるまでの間に設定した蒸煮条件に沿うように、蒸煮
される。換言すれば、米5は設定した蒸煮条件に合うようにタンク2内に滞留することに
なる。この滞留時間は、米のアルファー化度、浸漬後の米の水分値、米の銘柄、新米か古
米か、蒸気圧及び蒸煮温度などのファクターにより大きく変わる。
On the other hand, the rice 5 is cooked so as to follow the cooking conditions set by the rotating blade 21 and the hollow blade 21a until the rice 5 is discharged from the outlet 30 of the discharge pipe 7 after being put into the tank 2. Is done. In other words, the rice 5 stays in the tank 2 so as to meet the set steaming conditions. This residence time varies greatly depending on factors such as the degree of alpha conversion of rice, the moisture content of the rice after soaking, the brand of the rice, whether it is new or old, steam pressure and cooking temperature.

そして、排出管7中を通過して出口30の端面30aに到達した蒸煮米5aは、出口3
0近傍で満管状態となってから出口30より排出する。以後、タンク2内に米5を適量投
入し続ければ、その投入量に見合った蒸煮米5aが連続して得ることが出来る。なお、蒸
煮米5aを一定量ずつ容器に収容したい場合は、容器に一定量の蒸煮米5aを収容した時
点で、例えば、中空スパイラル構造体6あるいは6aを設定時間作動させた時点(中空ス
パイラル構造体の形状、回転数、回転時間により蒸煮米5aの供給量を設定出来る)で、
出口30の端面30aを切出板などで蒸煮米5aをすり切りすると共に一旦塞ぎ、この塞
いでいる間に蒸煮米5aを収容している容器を空の容器に代えて、再び出口30を開けて
空の容器に蒸煮米5aを収容する。以後、同じ操作を続ければ良い。なお、出口30の端
面30aに蒸煮米5aが満管状態となっていて、しかも切出板などで出口30の端面30
aに沿い蒸煮後の蒸煮米5aをすり切りするから、端面30aにある蒸煮物5aに凹凸が
生じず、蒸煮米5aを正確に計量することが出来る。
And the steamed rice 5a that has passed through the discharge pipe 7 and reached the end face 30a of the outlet 30 is the outlet 3
After reaching a full state in the vicinity of 0, it is discharged from the outlet 30. Thereafter, if an appropriate amount of rice 5 is continuously fed into the tank 2, steamed rice 5a corresponding to the amount of the rice 5 can be obtained continuously. When it is desired to store the cooked rice 5a in a container by a certain amount, for example, when a certain amount of the cooked rice 5a is stored in the container, for example, when the hollow spiral structure 6 or 6a is operated for a set time (hollow spiral structure). The supply amount of steamed rice 5a can be set according to the shape of the body, the number of rotations, and the rotation time)
The end surface 30a of the outlet 30 is cut through the cooked rice 5a with a cutting plate or the like, and once closed, the container containing the cooked rice 5a is replaced with an empty container and the outlet 30 is opened again. The steamed rice 5a is accommodated in an empty container. Thereafter, the same operation may be continued. Note that the steamed rice 5a is in a full tube state on the end face 30a of the outlet 30, and the end face 30 of the outlet 30 is cut out by a cutting plate or the like.
Since the steamed rice 5a after cooking is cut along a, the unevenness does not occur in the steamed product 5a on the end face 30a, and the steamed rice 5a can be accurately measured.

次に、図1乃至3に示す連続蒸煮装置において、中空スパイラル構造体の実効長さL=
592mm、羽根の外径D1=140mm、中空軸の外径D2=75mm、羽根のピッチ
=100mmであり、中空スパイラル構造体の回転数10rpm、蒸気温度100℃、蒸
気圧1.2Kg/cm2 、蒸煮時間10分間、米の供給量600kg/時間とした。この
条件で、(1)生米、(2)1時間浸漬後の米、(3)3時間浸漬後の米、をそれぞれ蒸
煮にした。更に、(4)(3)3時間浸漬後の米を1時間蒸煮した。得られた各蒸煮米に
ついて、グルコアミラーゼ法(日本食品工業学会:食品分析法646−649(1982
年))により、それぞれ糊化度を測定した。その結果、(1)の生米の糊化度は36.7
、(2)の蒸煮米の糊化度は76.6、(3)の蒸煮米の糊化度は81.6であり、(4
)の蒸煮米の糊化度は86.2であった。よって、本連続蒸煮装置により、必要とする糊
化度の米を得ることが出来た。
Next, in the continuous cooking apparatus shown in FIGS. 1 to 3, the effective length L =
592 mm, blade outer diameter D1 = 140 mm, hollow shaft outer diameter D2 = 75 mm, blade pitch = 100 mm, rotation speed of hollow spiral structure 10 rpm, steam temperature 100 ° C., steam pressure 1.2 Kg / cm 2 , The steaming time was 10 minutes, and the supply rate of rice was 600 kg / hour. Under these conditions, (1) fresh rice, (2) rice after 1 hour immersion, and (3) rice after 3 hour immersion were each cooked. Furthermore, (4) (3) the rice after 3 hours immersion was cooked for 1 hour. About each obtained cooked rice, the glucoamylase method (Japan Food Industry Association: Food analysis method 646-649 (1982)
Year)), the degree of gelatinization was measured respectively. As a result, the gelatinization degree of the raw rice of (1) is 36.7.
The degree of gelatinization of the cooked rice of (2) is 76.6, the degree of gelatinization of the cooked rice of (3) is 81.6, (4
) Of steamed rice was 86.2. Therefore, the rice of the gelatinization degree required by this continuous cooking apparatus was able to be obtained.

以上、本発明の実施例1を説明したが、具体的な構成はこれに限定されず、例えば、中
空スパイラル構造体は通常のスクリュータイプであるが、蒸煮対象物を搬送しつつかき混
ぜ作用の顕著なリボンスクリュータイプでも適用可能であり、また、蒸煮についてのみ説
明したが、殺菌、殺虫にも対応できることは言うまでもなく、本発明の要旨を逸脱しない
範囲での変更は適宜可能であることは理解されるべきである。
As mentioned above, although Example 1 of this invention was demonstrated, a specific structure is not limited to this, For example, although a hollow spiral structure is a normal screw type, it is remarkable of a stirring action, conveying a steaming target object. However, it is understood that modifications can be made as appropriate without departing from the spirit of the present invention. Should be.

本発明の連続蒸煮装置は、蒸煮対象物の蒸煮条件が厳しく、しかも蒸煮条件を種々変え
て性状の異なる蒸煮物を得たり、一定量ずつ容器に収容したり単に連続的に蒸煮物を得た
いなどの場合に、利用可能性が極めて高くなる。
The continuous steaming apparatus of the present invention has strict steaming conditions for the object to be steamed, and various steaming conditions can be obtained to obtain steamed foods having different properties, or can be accommodated in containers in a certain amount or simply to obtain steamed foods continuously. In such a case, the availability becomes extremely high.

本発明の実施の形態を示す連続蒸煮装置の正面図である(実施例1)。It is a front view of the continuous cooking apparatus which shows embodiment of this invention (Example 1). 本発明の実施の形態を示す連続蒸煮装置の平面図である(実施例1)。It is a top view of the continuous cooking apparatus which shows embodiment of this invention (Example 1). 本発明の実施の形態を示す連続蒸煮装置の側面図である(実施例1)。It is a side view of the continuous cooking apparatus which shows embodiment of this invention (Example 1). 連続蒸煮装置のタンクを示す正面図である(実施例1)。It is a front view which shows the tank of a continuous cooking apparatus (Example 1). 連続蒸煮装置のタンクを示す側面図である(実施例1)。It is a side view which shows the tank of a continuous cooking apparatus (Example 1). 連続蒸煮装置の中空スパイラル構造体を示す平面図である(実施例1)。It is a top view which shows the hollow spiral structure of a continuous cooking apparatus (Example 1). 連続蒸煮装置の中空スパイラル構造体の他の形状を示す平面図である(実施例1)。It is a top view which shows the other shape of the hollow spiral structure of a continuous cooking apparatus (Example 1). 従来例を示す断面図である。It is sectional drawing which shows a prior art example. 従来例を示す側方から見た概略の概念図である。It is the schematic conceptual diagram seen from the side which shows a prior art example. 従来例を示す断面図である。It is sectional drawing which shows a prior art example. 従来例を示す断面図である。It is sectional drawing which shows a prior art example.

符号の説明Explanation of symbols

1 連続蒸煮装置
2,a タンク
3 底部
4,18a,e 蒸気吹出開口
5 蒸煮対象物(米)
5a 蒸煮物(蒸煮米)
6,6a 中空スパイラル構造体
7,r 排出管
8 覗き窓
9 ドレーン弁
10 フランジ
11 板
12 蒸気排出室
13 蒸気排出管
14,p 底板
15,q 側板
16 蒸気排出口
17 蒸気ヘッダー
17a パイプ
18 蒸気供給パイプ
19 調整弁
20 中空軸
21 羽根
21a 中空羽根
30,s 出口
30a 端面
31 曲管
32 直管
b スクリュー
c 排出樋
d 排出口
f 蒸気管
g 機体
h ネットコンベア
i 蒸気供給室
j 下壁面
k 蒸煮路
m 供給口
n 扉
o 切出具
DESCRIPTION OF SYMBOLS 1 Continuous cooking apparatus 2, a Tank 3 Bottom part 4,18a, e Steam blowing opening 5 Steaming target object (rice)
5a Steamed food (steamed rice)
6, 6a Hollow spiral structure 7, r Discharge pipe 8 Viewing window 9 Drain valve 10 Flange 11 Plate 12 Steam discharge chamber 13 Steam discharge pipe 14, p Bottom plate 15, q Side plate 16 Steam discharge port 17 Steam header 17a Pipe 18 Steam supply Pipe 19 Adjusting valve 20 Hollow shaft 21 Blade 21a Hollow blade 30, s Outlet 30a End surface 31 Curved tube 32 Straight tube b Screw c Discharge rod d Discharge port f Steam tube g Machine body h Net conveyor i Steam supply chamber j Lower wall k Steaming path m Supply port n Door o Cutting tool

Claims (9)

タンク内の底部に、複数の蒸気吹出開口を有すると共に蒸煮対象物をほぼ定量搬送可能
な中空スパイラル構造体を回転自在に軸支し、且つ該中空スパイラル構造体の排出管を前
記タンクの側面から延出して設けてなり、前記タンク内に投入された蒸煮対象物に、前記
中空スパイラル構造体を回転させた状態で、前記蒸気吹出開口からの蒸気を供給すると共
に、蒸煮対象物を前記排出管側に搬送するようにしたことを特徴とする連続蒸煮装置。
A hollow spiral structure having a plurality of steam outlets at the bottom of the tank and capable of almost quantitatively conveying the object to be cooked is rotatably supported, and a discharge pipe of the hollow spiral structure is provided from the side of the tank. In the state where the hollow spiral structure is rotated, the steam from the steam outlet opening is supplied to the steaming target object provided in the tank, and the steaming target object is supplied to the discharge pipe. Continuous steaming device characterized in that it is conveyed to the side.
前記タンクの底板及び側板の少なくと底板に、蒸気排出口を複数設けて、蒸煮対象物を
蒸煮処理した後の過剰な蒸気を前記タンク内から外部に排除することを特徴とする請求項
1記載の連続蒸煮装置。
2. A plurality of steam discharge ports are provided in at least a bottom plate and a side plate of the tank, and excess steam after steaming a steaming object is excluded from the inside of the tank. Continuous cooking equipment.
前記中空スパイラル構造体は中空軸と羽根とからなり、前記中空軸に前記蒸気吹出開口
を複数開けてなることを特徴とする請求項1または2記載の連続蒸煮装置。
The continuous cooking apparatus according to claim 1 or 2, wherein the hollow spiral structure includes a hollow shaft and blades, and a plurality of the steam blowing openings are formed in the hollow shaft.
前記羽根は中空であり、該中空羽根に前記蒸気吹出開口を複数開けてなることを特徴と
する請求項3記載の連続蒸煮装置。
The continuous steaming apparatus according to claim 3, wherein the blade is hollow, and a plurality of the steam blowing openings are formed in the hollow blade.
前記中空スパイラル構造体の前記羽根の外径(D1)と前記中空軸の外径(D2)との
比率(D1/D2)は、1.1乃至15としたことを特徴とする請求項3または4記載の
連続蒸煮装置。
The ratio (D1 / D2) between the outer diameter (D1) of the blade of the hollow spiral structure and the outer diameter (D2) of the hollow shaft is 1.1 to 15, or 4. Continuous cooking apparatus according to 4.
前記羽根の外径(D1)と前記中空スパイラル構造体の実効長さ(L)との比率(D1
/L)は、0.1乃至10としたことを特徴とする請求項3乃至5のいずれか1項記載の
連続蒸煮装置。
Ratio (D1) between the outer diameter (D1) of the blade and the effective length (L) of the hollow spiral structure
6. The continuous cooking apparatus according to any one of claims 3 to 5, wherein / L) is 0.1 to 10.
前記排出管はその出口側を上方に湾曲させてなり、前記排出管の出口の端面中心部は、
前記中空スパイラル構造体の軸心よりも、前記羽根の外径(D1)の0.1乃至5倍垂直
方向に高く位置するようにしたことを特徴とする請求項3乃至6のいずれか1項記載の連
続蒸煮装置。
The discharge pipe has its outlet side curved upward, and the center of the end face of the outlet of the discharge pipe is
7. The method according to claim 3, wherein the hollow spiral structure is positioned higher in the vertical direction by 0.1 to 5 times the outer diameter (D1) of the blade than the axial center of the hollow spiral structure. The continuous cooking apparatus as described.
前記排出管は、前記中空スパイラル構造体の前記羽根の外径(D1)に対して1乃至5
0mmのクリアランスを有し、且つ前記中空スパイラル構造体の実効長さ(L)の0.0
1乃至2.0倍の長さを有することを特徴とする請求項3乃至7のいずれか1項記載の連
続蒸煮装置。
The discharge pipe is 1 to 5 with respect to the outer diameter (D1) of the blade of the hollow spiral structure.
0.0 mm of the effective length (L) of the hollow spiral structure having a clearance of 0 mm
The continuous cooking apparatus according to any one of claims 3 to 7, wherein the continuous cooking apparatus has a length of 1 to 2.0 times.
蒸煮対象物の蒸煮温度は、前記中空スパイラル構造体に供給する蒸気の温度を変えるこ
とにより、制御するようにしたことを特徴とする請求項1乃至8のいずれか1項記載の連
続蒸煮装置。
The continuous cooking apparatus according to any one of claims 1 to 8, wherein the cooking temperature of the cooking object is controlled by changing a temperature of steam supplied to the hollow spiral structure.
JP2005247316A 2005-08-29 2005-08-29 Continuous steaming apparatus Pending JP2007061140A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2005247316A JP2007061140A (en) 2005-08-29 2005-08-29 Continuous steaming apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2005247316A JP2007061140A (en) 2005-08-29 2005-08-29 Continuous steaming apparatus

Publications (1)

Publication Number Publication Date
JP2007061140A true JP2007061140A (en) 2007-03-15

Family

ID=37924056

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2005247316A Pending JP2007061140A (en) 2005-08-29 2005-08-29 Continuous steaming apparatus

Country Status (1)

Country Link
JP (1) JP2007061140A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109592318A (en) * 2018-11-21 2019-04-09 衡阳雄伟运输机械有限公司 Tube-type spiral conveyer intermediate support connector transition structure
CN115500530A (en) * 2022-10-14 2022-12-23 湖州中江纺织机械有限公司 A cooking equipment for producing fodder of raising silkworms

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS618014A (en) * 1984-06-21 1986-01-14 オ−ケ−食品工業株式会社 Soymilk boiling apparatus
JPS6286890U (en) * 1985-11-22 1987-06-03
JP2003088310A (en) * 2001-09-18 2003-03-25 Arai Kikai Seisakusho:Kk Vertical type steamer for making rice confectionery
JP2004033479A (en) * 2002-07-03 2004-02-05 Tiger Vacuum Bottle Co Ltd Rice supplying means for full automatic rice cooker and full automatic rice cooker using the same

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS618014A (en) * 1984-06-21 1986-01-14 オ−ケ−食品工業株式会社 Soymilk boiling apparatus
JPS6286890U (en) * 1985-11-22 1987-06-03
JP2003088310A (en) * 2001-09-18 2003-03-25 Arai Kikai Seisakusho:Kk Vertical type steamer for making rice confectionery
JP2004033479A (en) * 2002-07-03 2004-02-05 Tiger Vacuum Bottle Co Ltd Rice supplying means for full automatic rice cooker and full automatic rice cooker using the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109592318A (en) * 2018-11-21 2019-04-09 衡阳雄伟运输机械有限公司 Tube-type spiral conveyer intermediate support connector transition structure
CN115500530A (en) * 2022-10-14 2022-12-23 湖州中江纺织机械有限公司 A cooking equipment for producing fodder of raising silkworms
CN115500530B (en) * 2022-10-14 2023-06-02 湖州中江纺织机械有限公司 A cooking equipment for producing feed of raising silkworms

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