JPH07108260B2 - Continuous rice cooker - Google Patents

Continuous rice cooker

Info

Publication number
JPH07108260B2
JPH07108260B2 JP5214591A JP21459193A JPH07108260B2 JP H07108260 B2 JPH07108260 B2 JP H07108260B2 JP 5214591 A JP5214591 A JP 5214591A JP 21459193 A JP21459193 A JP 21459193A JP H07108260 B2 JPH07108260 B2 JP H07108260B2
Authority
JP
Japan
Prior art keywords
rice
steam
section
steaming
conveyor
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.)
Expired - Fee Related
Application number
JP5214591A
Other languages
Japanese (ja)
Other versions
JPH06181842A (en
Inventor
義弘 是澤
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.)
AIHOO KK
KORESAWA TETSUKOSHO KK
Original Assignee
AIHOO KK
KORESAWA TETSUKOSHO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by AIHOO KK, KORESAWA TETSUKOSHO KK filed Critical AIHOO KK
Priority to JP5214591A priority Critical patent/JPH07108260B2/en
Publication of JPH06181842A publication Critical patent/JPH06181842A/en
Publication of JPH07108260B2 publication Critical patent/JPH07108260B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Commercial Cooking Devices (AREA)
  • Cereal-Derived Products (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は弁当仕出し業、給食会
社、外食産業等の大量に炊飯を行う分野に好適に利用さ
れる連続式炊飯装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous type rice cooker suitable for use in a large number of rice cookers such as a lunch box catering business, a catering company, and a restaurant industry.

【0002】[0002]

【従来の技術】この種連続式炊飯装置の最新の従来技術
としては特開昭60−12945号公報に示されたもの
がある。
2. Description of the Related Art The latest prior art of this type of continuous rice cooking device is disclosed in Japanese Patent Laid-Open No. 12945/1985.

【0003】この装置は、水中浸漬処理された米粒をベ
ルトコンベヤで移送しながら蒸す一次蒸し部と、一次蒸
し部より送り込まれた米粒をスクレーパコンベヤで順次
移送しながら水中で浸漬処理する二次浸漬部と、二次浸
漬部で浸漬された米粒を更にベルトコンベヤで移送しな
がら二次蒸しを行う二次蒸し部を備えたものである。
This apparatus is a secondary soaking process in which rice grains soaked in water are transported by a belt conveyor while being steamed, and rice grains sent from the primary steaming unit are sequentially transported by a scraper conveyor in water. Part, and a secondary steaming part for performing secondary steaming while further transporting the rice grains soaked in the secondary dipping part by a belt conveyor.

【0004】この最新の従来技術によれば、大量の米を
一度に連続して炊飯できる利点があるが、米飯の食味
(旨み)の点で劣る難点がある。
According to this latest conventional technique, there is an advantage that a large amount of rice can be continuously cooked at one time, but there is a drawback that the taste (taste) of cooked rice is inferior.

【0005】この種炊飯装置は、大量処理を効率的に行
うことも重要であるが、それよりも最も重要なことは炊
飯される米飯の食味をいかに良くするかにつきる。たと
え大量処理できても、米飯の食味がまずければ全く用を
なさない。
It is important for this kind of rice cooker to efficiently perform a large amount of processing, but the most important thing is to improve the taste of cooked rice. Even if it can be processed in large quantities, if the cooked rice has a bad taste, it is useless.

【0006】そこで本発明をよく理解するために、まず
米飯の食味に関する理論を説明し、その上で本発明の特
徴について述べる。
Therefore, in order to understand the present invention well, first, the theory of the taste of cooked rice will be explained, and then the characteristics of the present invention will be described.

【0007】米飯の食味(これをテクスチャー、textur
e )は、硬さ、粘り、弾力性の3要素のバランスにある
と云われ、特に米飯の食味(旨み)の要素は圧倒的に硬
さと粘りに関係し両者が互にバランスを保っていること
が絶対に必要である。多少硬めの米飯(ゴハン)でも、
硬さに比例した粘り強さがあれば、一応旨いゴハンとい
えるし、同じ硬めのゴハンでも粘りが少し足りない場合
には、バランスがくずれているので旨くない範囲に入
る。
The taste of cooked rice (texture, textur
e) is said to be in a balance of three factors of hardness, tenacity and elasticity, and in particular, the element of the taste (taste) of cooked rice is overwhelmingly related to hardness and tenacity, and both maintain a balance between each other. Is absolutely necessary. Even a little hard rice,
If it has a tenacity proportional to hardness, it can be said that it is a good gohan, and if the toughness of the same hardness is not enough, the balance is broken and it falls into a bad range.

【0008】このように米飯の上記3要素のバランスを
良好に保つためには、米の水に浸漬する時間、加水量、
蒸らしの方法と時間を考慮する必要がある。
As described above, in order to maintain a good balance among the above-mentioned three factors of cooked rice, the time of dipping rice in water, the amount of water added,
It is necessary to consider the steaming method and time.

【0009】そして上記浸漬工程では、米飯は水分を吸
収して膨潤すると共に、米飯の味を良くするデキストリ
ン、遊離アミノ酸、遊離糖が含まれるデンプン質成分が
溶出して糊化液となり、これが米飯に吸収されることに
なるが、しかしこの浸漬工程で水分が必要以上に吸収さ
れると食味に最も重要な要素である米飯の硬さが失われ
ることになる。
In the soaking step, the cooked rice absorbs water and swells, and at the same time, the starchy components containing dextrin, free amino acids and free sugar, which improve the taste of the cooked rice, are eluted to form a gelatinizing solution, which is cooked rice. However, if water is absorbed more than necessary in this soaking step, the hardness of cooked rice, which is the most important factor for eating quality, will be lost.

【0010】このため、この浸漬工程では、最終工程
(蒸らし工程)における食味を最も良好な状態の水分の
吸収量を100%とすれば、85〜90%にとどめ、米
飯の硬さが壊れない状態に維持する必要がある。
For this reason, in this dipping process, if the moisture absorption in the final state (steaming process) is 100%, the moisture content in the best taste is 85-90%, and the hardness of the cooked rice is not broken. Need to be kept in a state.

【0011】上述のように浸漬工程でデンプン質糊化液
が米粒に吸収されることになるが、このとき水分が必要
以上に吸収されると米粒の硬さが失われることになる。
As described above, the starch gelatinization liquid is absorbed by the rice grains in the dipping process, but if moisture is absorbed more than necessary at this time, the hardness of the rice grains will be lost.

【0012】したがってこの浸漬工程では、デンプン質
糊化液は米粒に十分に吸収されるが、水分は必要以上に
吸収されない構成に形成しなければならない。
Therefore, in this dipping step, the starchy gelatinizing liquid must be formed so as to be sufficiently absorbed by the rice grains but not absorb water more than necessary.

【0013】しかもこのデンプン質糊化液が米粒に吸収
されることによって後続の蒸らし工程で十分に混練する
ことによって十分な粘りを生ぜしめることになる。
Moreover, the starchy gelatinizing liquid is absorbed by the rice grains, so that it is sufficiently kneaded in the subsequent steaming step to produce sufficient stickiness.

【0014】即ち、二次蒸し部ではほぐし機によって米
粒を十分に混練し、米粒相互の粘りを生ぜしめる必要が
あるが、従来装置ではこの点の配慮もないため一層食味
が劣る難点があった。
That is, in the secondary steaming section, it is necessary to sufficiently knead the rice grains by a loosening machine so that the rice grains become sticky to each other, but the conventional apparatus has a problem that the taste is further inferior because there is no consideration for this point. .

【0015】また浸漬工程(二次浸漬部)で食味及び粘
りに最も影響するデンプン質糊化液を米粒に十分に吸収
させる必要があるが、この際必要以上に水分を米粒に吸
収させると食味に最も重要な要素である米粒の硬さが失
われることになる。
In the dipping process (second dipping portion), it is necessary to allow the rice grains to sufficiently absorb the starchy gelatinizing liquid, which has the greatest influence on the taste and stickiness. The hardness of the rice grain, which is the most important factor, will be lost.

【0016】したがってこの浸漬工程では上述の二律背
反する命題をいかに合理的に解決するかによって米飯の
食味に大きな影響を与えることになり、この種炊飯装置
の成否は、この浸漬工程の処理にあるといっても過言で
はない。
Therefore, in this dipping step, the taste of cooked rice will be greatly affected by how to rationally solve the above contradictory proposition, and the success or failure of this type of rice cooker lies in the treatment of this dipping step. It's no exaggeration to say.

【0017】従来装置では、特にこの浸漬工程(二次浸
漬部)での処理が不十分、不完全であったため食味の良
い米飯を製造することができなかった。
In the conventional apparatus, particularly in this dipping process (secondary dipping portion), the treatment was insufficient and incomplete, so that cooked rice with a good taste could not be produced.

【0018】更に具体的に上記従来技術の要部を図面を
参照して説明すれば、図9は従来技術の二次浸漬部39
の終端部を示すもので、40は加熱水槽で、この加熱水
槽40に沿ってスクレーパコンベヤ41がプーリ42に
よって懸架されている。加熱水槽40の終端部底壁40
aはスクレーパコンベヤ41の回動軌跡に沿って円弧状
に形成され、加熱水は終端部上縁40bのレベルまで充
填されている。加熱水槽40内の米粒3はスクレーパコ
ンベヤ41で押圧され、その移送途上においてα化と吸
水膨潤化が進行し、その終端部でスクレーパコンベヤ4
1によって次の二次蒸し部43に送り込まれることにな
るが、この従来技術では加熱水槽40内の米粒3がスク
レーパコンベヤ41に押圧され、その終端部上縁40b
を乗り越えて移送される際に、水切り部がないため水分
の多量に含んだまま移送されることになる。
More specifically, the main part of the prior art will be described with reference to the drawings. FIG. 9 shows the secondary dipping portion 39 of the prior art.
The heating water tank 40 has a scraper conveyor 41 suspended by a pulley 42 along the heating water tank 40. Bottom wall 40 at the end of the heated water tank 40
A is formed in an arc shape along the rotation trajectory of the scraper conveyor 41, and the heated water is filled up to the level of the upper edge 40b of the end portion. The rice grains 3 in the heating water tank 40 are pressed by the scraper conveyor 41, and α and swelling by water absorption progress during the transfer, and the scraper conveyor 4 at the end thereof.
1, the rice grains 3 in the heating water tank 40 are pressed by the scraper conveyor 41, and the upper edge 40b of the end portion thereof is sent to the secondary steaming portion 43.
When there is no water drainage part when it is transferred over the water, it will be transferred while containing a large amount of water.

【0019】このため、米粒は二次浸漬部で水分を必要
以上に吸収されその硬さが失われることになり、更には
多量の水分と共に二次蒸し部に移送されるため、二次蒸
し部での加水が必要以上に多くなると共に、多量の水分
が二次蒸し部のベルトコンベヤのメッシュ目等から下方
に一度に落下し、これにより米粒に付着しているデンプ
ン糊化成分が外部に洗い流され、このため米粒の粘りが
なくなり、食味を一層悪くする難点があった。
Therefore, the rice grains absorb more water than necessary in the secondary soaking section and lose their hardness. Further, since the rice grains are transferred to the secondary steaming section together with a large amount of water, the secondary steaming section. The amount of water added in the steaming process becomes unnecessarily large, and a large amount of water drops downward from the meshes of the belt conveyor in the secondary steaming section all at once, which causes the starch gelatinization components adhering to the rice grains to be washed out to the outside. As a result, the stickiness of the rice grains disappears, and there is a problem that the taste is worsened.

【0020】さらに上記従来装置では、その移送状態が
不均一であるため、二次浸漬部における吸水ムラ及び二
次蒸し部における蒸しムラの発生する難点があり、その
蒸煮状態が不完全であった。
Further, in the above conventional apparatus, since the transfer state is non-uniform, there is a problem that water absorption unevenness in the secondary immersion part and steaming unevenness in the secondary steaming part occur, and the steaming state is incomplete. .

【0021】即ち予め水中浸漬処理された米粒を一次蒸
し部によって一次蒸しすることによって米はある程度α
化と糊化が進行し米粒間が付着して一次蒸し部終端では
米粒の半塊の状態になっている。したがって上記従来装
置のようにこの状態のまま、次の二次浸漬部に送り込め
ば米粒の塊がそのまま大小の塊となって断続的に二次浸
漬部に移送されることになり、二次浸漬部に定量宛送ら
れないことになると共に、米粒の塊の状態で移送される
ため塊の中心部分の米粒には充分な吸水効果をもたせる
ことができない。
That is, rice is preliminarily α
The saccharification and gelatinization proceed, and the rice grains adhere to each other, resulting in a half-lump of rice grains at the end of the primary steaming section. Therefore, if it is sent to the next secondary dipping section in this state as in the above conventional apparatus, the lumps of rice grains will be directly transferred to the secondary dipping section as large and small lumps. Since it is not sent to the dipping portion in a fixed amount, the rice grains in the central portion of the lump cannot have a sufficient water absorbing effect because they are transferred in the state of lumps of rice grains.

【0022】また二次浸漬部で浸漬され、更に糊化と吸
水膨潤化が進行した米粒がスクレーパコンベヤに押圧さ
れて移送される際に二次浸漬部終端では該コンベヤには
糊化した多量の米粒が塊状に付着することになるが、上
記従来装置ではこの状態のまま次の二次蒸し部に送り込
まれることになるため、米粒の送り量が更に断続的にな
って二次蒸し部のベルトコンベヤに堆積される米粒の堆
積厚が移送方向に凹凸状となって蒸気の通過量が不均一
となり蒸しムラの原因とあると共に、スクレーパコンベ
ヤに付着した米の塊が再び二次浸漬部に還流されてここ
で完全に糊化されてしまい、これによって二次浸漬部の
水分が糊の混濁液と化し、この糊状混濁液が米粒の表面
に被膜状に付着し、この被膜が吸水効果を一層減少せし
め吸水ムラの原因となったり米粒の芯まで吸水されない
ため、二次蒸し部を通過しても芯部のα化が充分に達成
されないため芯のある歯ざわりの悪い仕上りとなってい
た。
Further, when the rice grains that have been dipped in the secondary dipping section and further gelatinized and swollen by water absorption are pressed and transferred to the scraper conveyor, a large amount of gelatinized on the conveyor at the end of the secondary dipping section. Although rice grains will adhere in a lump form, in the above-mentioned conventional device, since it will be sent to the next secondary steaming section in this state, the feed amount of rice grains becomes more intermittent and the belt of the secondary steaming section becomes The accumulated thickness of rice grains accumulated on the conveyor becomes uneven in the transfer direction, resulting in non-uniform steam flow, causing steaming unevenness, and the lumps of rice adhering to the scraper conveyor flow back to the secondary dipping section. Then, it is completely gelatinized here, whereby the water in the secondary immersion part becomes a turbid liquid of glue, and this glutinous turbid liquid adheres to the surface of the rice grain in a film form, and this film has a water absorbing effect. Cause of uneven water absorption For it or not water until the rice grains of the core, has been a crunchy bad finish with a core for α of the core portion is also passed through the secondary steamed part is not sufficiently achieved.

【0023】また一次及び二次蒸し部は、蒸気をメッシ
ュベルトコンベヤ上の米粒群に吹き込んで蒸し作用を行
うようになっているが、従来では蒸気の米粒群に対する
吹き込みにバラツキがあり、所謂蒸しムラの原因にもな
っていた。
In the primary and secondary steaming sections, steam is blown into the rice grain groups on the mesh belt conveyor to perform steaming action. However, conventionally, there is variation in the amount of steam blown into the rice grain groups. It was also a cause of unevenness.

【0024】このように上記従来装置では米の蒸煮状態
が不完全で品質の良い製品を得ることができなかった。
As described above, in the above conventional apparatus, the steamed state of rice was incomplete and it was not possible to obtain a good quality product.

【0025】[0025]

【発明が解決しようとする課題】この発明は、この種連
続式炊飯装置において、上述の炊飯理論を忠実に実践す
ることによって、吸水ムラ及び蒸しムラをなくして均一
で品質の良い且つ食味(旨み)のよい米飯を製造するこ
とを目的とする。
The present invention, in this type of continuous rice cooker, faithfully practices the above-mentioned rice cooking theory to eliminate unevenness in water absorption and unevenness in steaming, and to provide a uniform and good taste (taste). ) Is intended to produce good cooked rice.

【0026】[0026]

【課題を解決するための手段】上記問題点を解決するた
めに、請求項1に係る発明にあっては、水中浸漬処理を
施した米の供給部と、供給される米を移送するメッシュ
ベルトコンベヤならびに移送中の米を蒸す加熱水蒸気の
吹出し口を備えた一次蒸し部と、この蒸し部から連続的
に供給される米を浸漬する加熱水槽ならびに該加熱水槽
中の米を移送するスクレーパコンベヤを備えた二次浸漬
部と、この浸漬部から連続的に供給される米を取出し部
まで移送するメッシュベルトコンベヤならびに移送中の
米を蒸す加熱水蒸気の吹出し口とを備えた二次蒸し部と
を有してなる連続式炊飯装置において、前記一次蒸し部
と前記二次蒸し部とにはそれぞれ上方が前記メッシュベ
ルトコンベヤに面して開口しコンベヤの移動方向に分割
された複数の蒸気室が設けられ、各蒸気室に上記コンベ
ヤの移動方向に直交する蒸気室幅方向全域にわたって蒸
気管が配設されると共に、各蒸気管には蒸気吹き出し口
が下向きに穿設され、前記複数の蒸気室は各底面の幅方
向片側が低くなるように傾斜し、且つ各蒸気室は上記底
面の低位側において互いに連通して排水管に連結されて
なる構成を採用するものである。
In order to solve the above-mentioned problems, in the invention according to claim 1, a rice supply section that has been subjected to immersion treatment in water, and a mesh belt for transferring the supplied rice. A conveyor and a primary steaming section equipped with an outlet for heating steam for steaming rice being transferred, a heating water tank for immersing rice continuously supplied from this steaming section, and a scraper conveyor for transferring the rice in the heating water tank A secondary steaming section provided with a secondary soaking section provided with, and a mesh belt conveyor for transferring the rice continuously supplied from this soaking section to the removing section, and an outlet for heated steam for steaming the rice being transferred. In a continuous rice cooker comprising, the primary steaming section and the secondary steaming section each have an upper opening facing the mesh belt conveyor and divided in the moving direction of the conveyor.
Multiple steam chambers are provided, and the above-mentioned
Steam over the entire width of the steam chamber orthogonal to the moving direction of the
A trachea is installed and each steam pipe has a steam outlet.
Are drilled downwards, and the plurality of steam chambers are the width of each bottom surface.
One side is inclined so that it is low, and each steam chamber is
On the lower side of the plane, communicating with each other and connected to the drain pipe
The following configuration is adopted.

【0027】[0027]

【0028】[0028]

【作用】請求項1に係る発明によれば、水中浸漬処理さ
れた米の供給部から一次蒸し部に供給された米粒はベル
トコンベヤによって順次連続的に移送され一次蒸し部終
端に至るまでに米粒はある程度α化と糊化が進行した状
態で次の二次浸漬部に送り込まれることになる。そし
て、二次浸漬部においてはスクレーパコンベヤに押圧さ
れて順次移送され、その移送途上において米粒に水分が
均一に吸収され、更にα化と吸水膨潤化が進行した状態
で二次浸漬部終端部の水面より上方に延びる傾斜面に移
送される。
According to the first aspect of the present invention, the rice grains fed from the rice soaked in the water to the primary steaming section are successively and continuously transferred by the belt conveyor until the end of the primary steaming section. Will be sent to the next secondary immersion part in a state where the gelatinization and gelatinization have progressed to some extent. Then, in the secondary dipping section, it is pressed by the scraper conveyor and sequentially transferred, and in the course of the transfer, moisture is uniformly absorbed in the rice grains, and in the state where α-formation and water swelling proceed further, the secondary dipping section end part It is transferred to an inclined surface extending above the water surface.

【0029】上記傾斜面を徐々に移送される間に米粒と
共に送られる不要な水分は側方より二次浸漬部に還流さ
れることになり、傾斜面上の米粒群には必要以上の水分
が吸収されることがなく、適度な硬さを保持することが
できる。
Unnecessary water which is sent together with the rice grains while being gradually transferred on the inclined surface is recirculated to the secondary dipping section from the side, and the rice particles on the inclined surface have more water than necessary. It is not absorbed and can maintain an appropriate hardness.

【0030】したがって傾斜面上には適量のデンプン糊
化液を含んだ米粒群のみが残留し、これらが徐々に移送
される途上でデンプン糊化液は米粒群に芯内部に至るま
で十分に吸収され、次の二次蒸し部の作用と相俟って粘
性と弾性を生ぜしめることになる。
Therefore, only the rice grain group containing an appropriate amount of starch gelatinization liquid remains on the inclined surface, and the starch gelatinization liquid is sufficiently absorbed by the rice grain group until the inside of the core while these rice grains are gradually transferred. Then, in combination with the action of the next secondary steaming part, viscousity and elasticity are produced.

【0031】このように上記傾斜面で不要な水分を除去
し、必要なデンプン糊化液を吸収した米粒群は二次蒸し
部に移送され、これらの米粒が適宜設けたほぐし機によ
ってほぐされ米粒に付着した糊化液中のデンプン細胞膜
が一部破壊され、味を良くするデキストリン、遊離アミ
ノ酸、遊離糖が浸出したデンプン質成分が米粒に十分に
混練されることによって米粒に、食味の上で重要な要素
の一つである粘りと照りを生ぜしめることになる。
As described above, the rice grain group from which the unnecessary water is removed on the inclined surface and the necessary starch gelatinization liquid is absorbed is transferred to the secondary steaming section, and the rice grains are loosened by an appropriate loosening machine. The starch cell membrane in the gelatinized liquid adhering to the part of the rice is partially destroyed, and the dextrin, free amino acid, and starchy components leached with free sugar, which improve the taste, are sufficiently kneaded into the rice grain to improve the taste. It will generate tenacity and shine, which are one of the important factors.

【0032】そして一次及び二次蒸し部には、それぞれ
上方が前記メッシュベルトコンベヤに面して開口しコン
ベヤの移動方向に分割された複数の蒸気室が設けられ、
各蒸気室に上記コンベヤの移動方向に直交する蒸気室幅
方向全域にわたって蒸気管が配設されてなるため、蒸気
室はその中心部も幅方向両端部も均等に蒸気が吹き出さ
れ、且つ各蒸気室に配設される蒸気管の蒸気吹き出し口
は下向きに開口しているため、該吹き出し口から吹き出
された蒸気は直接にベルトコンベヤ側に向かって吹き出
されるのではなく、各蒸気室の全壁面に向かって吹き出
され、蒸気を各蒸気室に一旦中継させて充満させたのち
に、各蒸気室の上方開口部に面する上記ベルトコンベヤ
のメッシュ孔より米粒群に蒸気を吹き込むようにしてい
るため、メッシュベルトコンベヤ上の米粒群に蒸気が
方向と送り方向とに均等に吹き込まれ、これがために蒸
しムラの発生なく良好の蒸し上がり状態となる。
The primary and secondary steaming sections are respectively opened on the upper side facing the mesh belt conveyor and connected to each other.
A plurality of steam chambers that are divided in the moving direction of the bayer are provided,
The width of the steam chamber in each steam chamber, which is orthogonal to the moving direction of the conveyor.
Since steam pipes are installed in all directions,
Steam is blown out evenly in the center of the chamber and at both ends in the width direction.
And, since the steam outlet of the steam pipe arranged in each steam chamber is opened downward, the steam blown out from the outlet is not directly blown toward the belt conveyor side, The steam is blown toward all the wall surfaces of each steam chamber, and after steam is once relayed to each steam chamber to fill it, steam is fed to the rice grain groups through the mesh holes of the belt conveyor facing the upper opening of each steam chamber. due to the way blown, steam width rice grains group on the mesh belt conveyor
It is blown evenly in both the feed direction and the feed direction , which results in a good steaming state without steaming unevenness.

【0033】また発明によれば、前記複数の蒸気室は
各底面の幅方向片側が低くなるように傾斜し、且つ各蒸
気室は上記底面の低位側において互いに連通して排水管
に連結されてなるため、各蒸気室で蒸気が冷却され凝縮
した凝縮液は速やかに外部に排出されることになり、加
熱エネルギーの熱損失を最小限に止めることができる。
[0033] According to the present invention, the plurality of steam chambers
Condensed liquid in which the steam is cooled and condensed in each steam chamber because the bottom of each bottom is inclined so that one side in the width direction is low, and each steam chamber is connected to the drain pipe in communication with each other on the lower side of the bottom. Will be quickly discharged to the outside, and the heat loss of heating energy can be minimized.

【0034】[0034]

【実施例】以下、この発明を図示実施例に基づいて説明
する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to illustrated embodiments.

【0035】図1で示すように、連続式炊飯装置1は、
ホッパー2より供給される一次浸漬処理を施した米粒3
をメッシュベルトコンベヤ4にて定速で移送しつつ蒸気
管5から吹き出す加熱水蒸気によって蒸す一次蒸し部A
と、この蒸し部Aから連続的に供給される米粒3を加熱
水槽6に浸漬した状態でスクレーパコンベヤ7にて移送
する二次浸漬部Bと、この浸漬部Bから連続的に供給さ
れる米粒3を一次蒸し部Aと同様にメッシュベルトコン
ベヤ8にて取出し部9まで定速で移送しつつ蒸気管5か
ら吹き出す加熱水蒸気によって蒸す二次蒸し部Cとから
構成されている。そして一次蒸し部Aにおけるメッシュ
ベルトコンベヤ4の後端に第1のほぐし機10aが、二
次蒸し部Cにおけるメッシュベルトコンベヤ8の前部に
第2のほぐし機10bが、またその中間部及び後端に同
様に第3及び第4のほぐし機10c, 10dが取付けら
れている。11はスクレーパコンベヤ7のスクレーパ板
12が加熱水槽6より離脱した位置でこれに加熱水を噴
射して洗浄するシャワー、13は加熱水槽6の水温を測
定する温度センサー、14は加熱水槽6のドレン、15
aはメッシュベルトコンベヤ4の後端においてメッシュ
ベルト4aに摺接して米粒をシュート16に落下させる
スクレーパ、15bはメッシュベルトコンベヤ8の後端
においてメッシュベルト8aに摺接して炊き上がった米
を取出し部9へ案内するスクレーパ、17aはメッシュ
ベルトコンベヤ4を駆動させる可変速モータ、17bは
スクレーパコンベヤ7と二次蒸し部Cの3基のほぐし機
10b, 10c, 10dを駆動させる可変速モータであ
る。なお、上記コンベヤ7と上記ほぐし機10b, 10
c, 10dとをそれぞれ別個の可変速モーターで駆動し
てもよいことは勿論である。17cはメッシュベルトコ
ンベヤ8を駆動させる可変速モータ、18は可変速モー
タ17bに連動するカム18aに接触してシャワー11
を間歇作動させるリミットスイッチである。
As shown in FIG. 1, the continuous rice cooker 1 is
Rice grain 3 that has been subjected to the primary dipping treatment supplied from hopper 2
Primary steaming section A in which the steam is blown from the steam pipe 5 while being transported by the mesh belt conveyor 4 at a constant speed.
And a secondary soaking section B in which the rice grains 3 continuously supplied from the steaming section A are immersed in the heated water tank 6 and transferred by the scraper conveyor 7, and rice grains continuously supplied from the soaking section B. Similarly to the primary steaming section A, the secondary steaming section C is composed of a mesh belt conveyor 8 and a secondary steaming section C where the steam is steamed from the steam pipe 5 while being transferred to the extraction section 9 at a constant speed. A first loosening machine 10a is provided at the rear end of the mesh belt conveyor 4 in the primary steaming section A, a second loosening machine 10b is provided in front of the mesh belt conveyor 8 in the secondary steaming section C, and an intermediate portion and a rear portion thereof. Similarly, third and fourth loosening machines 10c and 10d are attached to the ends. Reference numeral 11 is a shower for injecting heated water into the scraper plate 12 of the scraper conveyor 7 to separate it from the heated water tank 6 for cleaning, 13 is a temperature sensor for measuring the water temperature of the heated water tank 6, and 14 is a drain of the heated water tank 6. , 15
a is a scraper that slides on the mesh belt 4a at the rear end of the mesh belt conveyor 4 to drop the rice grains onto the chute 16, and 15b slides on the mesh belt 8a at the rear end of the mesh belt conveyor 8 to remove the cooked rice. The scraper for guiding to 9 is a variable speed motor 17a for driving the mesh belt conveyor 4, and 17b is a variable speed motor for driving the scraper conveyor 7 and the three loosening machines 10b, 10c, 10d of the secondary steaming section C. The conveyor 7 and the loosening machines 10b, 10
Of course, c and 10d may be driven by separate variable speed motors. Reference numeral 17c is a variable speed motor for driving the mesh belt conveyor 8, and 18 is a shower 11 which contacts a cam 18a which is interlocked with the variable speed motor 17b.
It is a limit switch that operates intermittently.

【0036】ホッパー2は、図2で示すように、蓋板2
aのフランジ状縁部に上端に固着したハンドル19aに
て回転するねじ軸19が垂設されており、このねじ軸1
9に螺合した昇降子19bに固着された板状シャッター
20をガイド板20aに沿って上下摺動させることによ
り、出口開口2aの上下方向開口幅を任意に調整し得る
ようにしてある。すなわちこの出口開口2aの開口幅と
メッシュベルトコンベヤ4の送り速度とを調整すること
によって米3の供給量が広範囲で調整できる。
The hopper 2, as shown in FIG.
A screw shaft 19 that rotates with a handle 19a fixed to the upper end is vertically installed at the flange-shaped edge portion of a.
By vertically sliding the plate-shaped shutter 20 fixed to the elevator 19b that is screwed to the plate 9 along the guide plate 20a, the vertical opening width of the outlet opening 2a can be adjusted arbitrarily. That is, the amount of rice 3 supplied can be adjusted in a wide range by adjusting the opening width of the outlet opening 2a and the feeding speed of the mesh belt conveyor 4.

【0037】一次蒸し部Aにおいて、メッシュベルトコ
ンベヤ4のメッシュベルト4aは目の細かいステンレス
製ネットなどから形成されており、図3および図4で示
すように上位側つまり往動側のベルト4aの下面側に上
方開放したケーシング板21とその内部を区割する仕切
り板22, 22…とから移送方向に沿って並ぶ複数の蒸
気室23が構成されている。またケーシング板21の両
側フランジ部21a,21aにそれぞれ垂直ガイド板2
4がその下部フランジ部24aにおいて固着されてお
り、上位側のベルト4aは両端縁部がそれぞれフランジ
部21aと24aとの間に僅かな間隙を余して挟まれる
ように配置している。そして各蒸気室23内に蒸気管5
の各分岐管5aが各蒸気室23の幅方向全域にわたって
水平に突入配置されており、この分岐管5aに所定間隔
で穿設された下向きの吹出し口25より噴出した加熱水
蒸気がメッシュベルト4aを通して、両側ガイド板2
4, 24間で移送されつつある米3の堆積層中に吹き込
まれ、蒸し作用が行われる。また各吹出し口25が下向
きに開口しているのは、蒸気管23が各蒸気室23の幅
方向全域にわたって配設されることと相まって、加熱水
蒸気が蒸気室23内に一旦充満してその上面全面から均
等に上記堆積層中に吹き込まれるようにし、局部的な蒸
し状態の過不足の発生を防止するためである。更に蒸気
室23の底面の幅方向片側が低くなるように傾斜し、か
つ複数の蒸気室23, 23…は上記傾斜の低位側におい
て仕切り板23に設けた開口22aを通して連通してお
り、各蒸気室23内で凝縮した水が上記傾斜の低位側に
集められて排水管26より排出されるようになされてい
る。27はアングル材等からなる取付け用枠組みであ
る。
In the primary steaming section A, the mesh belt 4a of the mesh belt conveyor 4 is formed of a fine mesh net made of stainless steel or the like, and as shown in FIGS. 3 and 4, the upper side, that is, the forward side belt 4a. A plurality of steam chambers 23 lined up in the transfer direction are formed by a casing plate 21 that is open upward on the lower surface side and partition plates 22, 22 that partition the inside thereof. In addition, the vertical guide plate 2 is attached to the flanges 21a on both sides of the casing plate 21, respectively.
4 are fixed to the lower flange portion 24a, and the upper belt 4a is arranged such that both edge portions thereof are sandwiched between the flange portions 21a and 24a with a slight gap left therebetween. Then, in each steam chamber 23, the steam pipe 5
Each of the branch pipes 5a is horizontally projected and arranged in the entire width direction of each steam chamber 23, and the heated steam ejected from the downward outlets 25 formed at predetermined intervals in the branch pipes 5a. Both side guide plates 2 through the mesh belt 4a
It is blown into the sediment layer of rice 3 being transferred between 4 and 24, and steaming action is performed. In addition, each outlet 25 is opened downward because the steam pipe 23 has a width of each steam chamber 23.
In addition to being arranged over the entire area in the direction, the heating steam is once filled in the steam chamber 23 so that the steam is uniformly blown into the above-mentioned deposition layer from the entire upper surface of the steam chamber 23. This is to prevent it. Further, the bottom surface of the steam chamber 23 is inclined so that one side in the width direction is lowered, and the plurality of steam chambers 23, 23 ... Are communicated with each other through the opening 22a provided in the partition plate 23 on the lower side of the inclination. The water condensed in the chamber 23 is collected on the lower side of the slope and discharged from the drain pipe 26. Reference numeral 27 is a mounting frame made of an angle member or the like.

【0038】以上のように一次蒸し部A及び後述の二次
蒸し部Cには、図3及び図4に示すように、それぞれ上
方が前記メッシュベルトコンベヤ4,8に面して開口
コンベヤの移動方向に分割された複数の蒸気室23が設
けられ、各蒸気室23に上記コンベヤ4,8の移動方向
に直交する蒸気室幅方向全域にわたって蒸気管5aが配
設されてなるため、蒸気室23にはその中心部も幅方向
両端部も均等に蒸気が吹き出され、且つ各蒸気室23に
配設される蒸気管5aの蒸気吹き出し口25は下向きに
開口しているため、該吹き出し口25から吹き出された
蒸気は直接にベルトコンベヤ側に向かって吹き出される
のではなく、各蒸気室の全壁面に向かって吹き出され、
蒸気を各蒸気室23に一旦中継させて充満させたのち
に、各蒸気室23の上方開口部に面する上記ベルトコン
ベヤ4,8のメッシュ孔より米粒群に蒸気を吹き込むよ
うにしているため、メッシュベルトコンベヤ4,8上の
米粒群に蒸気が幅方向と送り方向とに均等に吹き込ま
れ、これがために蒸しムラの発生なく良好の蒸し上がり
状態となる。
The above as the primary steaming unit A and below the secondary steamed unit C, as shown in FIG. 3 and FIG. 4, the upper respectively opened facing the mesh belt conveyor 4,8
A plurality of steam chambers 23 that are divided in the moving direction of the conveyor are provided, and the moving directions of the conveyors 4 and 8 are provided in each steam chamber 23.
The steam pipe 5a is distributed over the entire width of the steam chamber orthogonal to
Since it is installed, the center of the steam chamber 23 is also in the width direction.
Both ends are evenly blown with steam, and the steam outlets 25 of the steam pipes 5a arranged in the respective steam chambers 23 are open downward, so that the steam blown out from the outlets 25 is directly conveyed to the belt. Instead of being blown toward the conveyor side, it is blown toward the entire wall of each steam chamber ,
Steam mixture was allowed to fill in temporarily relayed to each steam chamber 23, because it is so as blowing steam into rice grains group than the mesh holes of the belt conveyor 4, 8 facing the upper opening of the steam chamber 23, The steam is uniformly blown into the rice grain groups on the mesh belt conveyors 4 and 8 in the width direction and the feeding direction , which results in a good steamed state without uneven steaming.

【0039】更には図3に示すように、前記複数の蒸気
室23は各底面23aの幅方向片側が低くなるように傾
斜し、且つ各蒸気室23は上記底面23aの低位側にお
いて開口22aを介して互いに連通し排水管26に連結
されてなるため、各蒸気室23で蒸気の一部が冷却され
凝縮して生成された凝縮液は速やかに排水管26を通し
て外部に排出されることになり、加熱エネルギーの熱損
失を最小限に止めることができる。
Further, as shown in FIG. 3, the plurality of steam chambers 23 are inclined so that one side in the width direction of each bottom surface 23a is lowered, and each steam chamber 23 has an opening 22a on the lower side of the bottom surface 23a. Since they are communicated with each other through the drain pipe 26 and are connected to the drain pipe 26, the condensate produced by cooling and condensing part of the steam in each steam chamber 23 is promptly discharged to the outside through the drain pipe 26. The heat loss of heating energy can be minimized.

【0040】一方、第1〜第4のほぐし装置10a〜1
0dは、図5で示すように、多数のピン28, 28が一
定間隔でかつ角度を変えて軸方向視放射状に植設された
筒状回転軸29を駆動支軸30と枢支軸31との間に水
平に架設してなり、該回転軸29の回転に伴って各ピン
28が順次に米粒3の堆積層中に入り込んでこれをほぐ
す作用とならす作用を行う。そしてこの回転は通常はコ
ンベヤ4, 8の送りと順方向でかつピン28先端の移動
速度がメッシュベルト4a, 8aの送り速度より早く、
好ましくは3倍程度となるように設定され、これにより
上記ほぐし及びならし作用と共に米粒3の送り補助作用
が発揮される。尚、ピン28は稼動中に付着堆積する米
かすを定期的に洗浄除去する必要があるため、回転軸2
9は一端に駆動支軸30の係止ピン30aに係合する割
り溝29aを設けると共に、他端に枢支軸31に嵌合し
得る摺動筒29bとこれを外方押出側に付勢するコイル
ばね29cとを設けることにより、両支軸30, 31に
対して容易に着脱し得る構造としてある。30bは駆動
支軸30の軸受、31bは枢支軸31の軸受、32はメ
ッシュベルトコンベヤ8の駆動プーリの取付け板であ
る。
On the other hand, the first to fourth loosening devices 10a to 1
As shown in FIG. 5, 0d is a cylindrical rotary shaft 29 in which a large number of pins 28, 28 are planted radially at a constant interval and at different angles, as viewed in the axial direction, as a drive support shaft 30 and a pivot support shaft 31. Are horizontally installed between the pins, and each pin 28 sequentially enters into the accumulated layer of the rice grains 3 as the rotating shaft 29 rotates, and acts to loosen the pin. This rotation is normally in the forward direction with the feed of the conveyors 4 and 8, and the moving speed of the tip of the pin 28 is faster than the feed speed of the mesh belts 4a and 8a.
It is preferably set to be about 3 times, whereby the feeding aid action of the rice grains 3 is exhibited together with the above-mentioned loosening and leveling action. It should be noted that the pin 28 needs to regularly wash and remove the rice dregs deposited and accumulated during the operation, so that the rotary shaft 2
9 is provided with a split groove 29a which engages with the locking pin 30a of the drive support shaft 30 at one end, and a sliding cylinder 29b which can be fitted into the pivot support shaft 31 at the other end and which is biased toward the outward pushing side. By providing the coil spring 29c, the structure can be easily attached to and detached from both the support shafts 30 and 31. Reference numeral 30b is a bearing of the drive support shaft 30, 31b is a bearing of the pivot support shaft 31, and 32 is a mounting plate of a drive pulley of the mesh belt conveyor 8.

【0041】二次浸漬部Bにおいて、加熱水槽6は前部
から中央部にかけた水平面6aとこれに連続する後部の
上向き傾斜面6bと該傾斜面から急速に垂下するガイド
面6cとからなり、該傾斜面6bは図示のように略20
〜40度の傾斜度に、またガイド面6cは傾斜面6bと
の間に50〜70度の傾斜度に形成され、更には加熱水
槽6内の水33の水面より高位に傾斜面6bが延びてお
り、該傾斜面6bは米粒群の水切りと米粒群の内部に含
まれるデンプン糊化液が米粒の芯内部に至るまで吸収さ
れるためのデンプン糊化液吸収工程の作用をも果たすよ
うになっている。そしてこの加熱水槽6内には、図6で
示すように、シュート16から連続した断面上向き開放
コ字形にガイド枠34が上記水平部6aと傾斜部6bに
沿う形で底面を密着して配置され、かつこのガイド枠3
4の外側を取り囲むように加熱用蒸気管35が水33中
に配設されており、図示の状態から明らかなように、外
側の室と、ガイド枠34を挟んで内側の米粒群の収容さ
れる室との間を加熱水が対流するようになっている。一
方、スクレーパコンベヤ7は、加熱水槽6の水平面6a
上で同高さに配置したそれぞれ各一対の従動プーリ7
a, 7bと水切り傾斜面6bの後端延長線上の高位に配
置した駆動プーリ7cとに平行2条の無端チェーン7
d, 7dが巻き掛けられ、したがって該コンベヤ7の終
端部下面7dは前記水切り兼用デンプン糊化液吸収用傾
斜面6bに沿って設けられ、その延長線上で反転するよ
うになっている。図7でも示すようにこれらチェーン7
d, 7d間にわたって所定間隔毎にL字状取付片12a
を介してスクレーパ板12がチェーン方向に対して直角
に取付けてある。そして各スクレーパ板12は、下側チ
ェーン位置でガイド枠34内を両側端および下端が米粒
の出入不能な程度の小間隙をもって通過するように設定
してある。尚、プーリ7aの回転軸36にはプーリ7e
が取付けられ、このプーリ7eを介して一次蒸し部Aの
第1のほぐし機10aが駆動される。
In the secondary immersion part B, the heating water tank 6 comprises a horizontal surface 6a extending from the front part to the central part, a rearward upward inclined surface 6b which is continuous with the horizontal surface 6a, and a guide surface 6c which droops rapidly from the inclined surface. The inclined surface 6b is approximately 20
The inclined surface 6b is formed at an inclination of -40 degrees and the guide surface 6c is formed at an inclination of 50 to 70 degrees between the guide surface 6c and the inclined surface 6b, and the inclined surface 6b extends higher than the water surface of the water 33 in the heated water tank 6. Therefore, the inclined surface 6b also functions as a starch gelatinizing liquid absorbing step for draining the rice grain group and absorbing the starch gelatinizing liquid contained in the rice grain group to the inside of the core of the rice grain. Has become. As shown in FIG. 6, a guide frame 34 having an open U-shaped cross section continuous from the chute 16 is disposed in the heated water tank 6 so as to closely contact the bottom surface along the horizontal portion 6a and the inclined portion 6b. And this guide frame 3
4, a heating steam pipe 35 is disposed in the water 33 so as to surround the outside thereof, and as is clear from the state shown in the drawing, the rice chambers inside the outer chamber and the guide frame 34 are accommodated. The heated water is convective between the room and the room. On the other hand, the scraper conveyor 7 is a horizontal surface 6a of the heated water tank 6.
Each pair of driven pulleys 7 arranged at the same height above
a, 7b and a drive pulley 7c arranged at a high position on the extension line of the rear end of the draining inclined surface 6b, two endless chains 7 parallel to each other
The lower surface 7d of the terminal end portion of the conveyor 7 is provided along the inclined surface 6b for absorbing the starch gelatinizing liquid that also serves as a water drainer, and is inverted on its extension. As shown in FIG. 7, these chains 7
L-shaped mounting pieces 12a at predetermined intervals over d and 7d
The scraper plate 12 is attached at right angles to the chain direction. Each scraper plate 12 is set so that both side ends and the lower end thereof pass through the guide frame 34 at a position of the lower chain with a small gap such that rice grains cannot move in and out. In addition, the pulley 7e is attached to the rotary shaft 36 of the pulley 7a.
Is attached, and the first loosening machine 10a of the primary steaming section A is driven via this pulley 7e.

【0042】シャワー11はスクレーパコンベヤ7の駆
動プーリ7cに近接する位置にあり、加熱水槽6より離
脱した各スクレーパ板12が該プーリ7cの周回位置で
扇形に開く姿勢をとった際に加熱水を噴射して該スクレ
ーパ板12表面に付着した米粒3を加熱水と共に二次蒸
し部C側に洗い落とす働きをする。この噴射は、各スク
レーパ板12の1ピッチ分の移動毎にカム18aが一回
転する設定にしておくことにより、カム18aに接触す
るリミットスイッチ18の信号を受けて上記1ピッチ毎
に一定時間だけ、例えば1ピッチ移動時間を1分とした
際に3〜6秒程度行われるようにしてある。
The shower 11 is located in the vicinity of the drive pulley 7c of the scraper conveyor 7, and when the scraper plates 12 separated from the heating water tank 6 take a fan-like attitude at the orbital position of the pulley 7c, they heat water. The rice grains 3 sprayed and adhered to the surface of the scraper plate 12 have a function of washing off to the secondary steaming portion C side together with the heating water. This injection is set such that the cam 18a makes one rotation every movement of each scraper plate 12 by one pitch, and the signal from the limit switch 18 contacting the cam 18a is received for each fixed pitch for a predetermined time. For example, when the 1-pitch moving time is 1 minute, it is performed for about 3 to 6 seconds.

【0043】二次蒸し部Cは、一次蒸し部Aと同様に構
成されているので各部の詳細は省略する。ただしこの二
次蒸し部Cでは炊き上がりないしこれに近い状態の柔ら
かな米粒が相互に粘着して固まり易くかつガイド板27
にも粘着して送り抵抗が大きくなるため、第2のほぐし
機10bを前部に、そして好ましくは中間部と後端の3
カ所に第3及び第4のほぐし機10c, 10dを設けて
ほぐしと米粒の堆積厚か均一になるようならし作用と共
に送り補助機能を高めている。これらほぐし機10b〜
10dはチェーンを介して3基が同期駆動する。またメ
ッシュベルトコンベヤ8の高さは、加熱水槽6から出て
来た水分含量の多い米3が落下の衝撃でつぶれるのを防
ぐため、加熱水槽6の後端ガイド片6cを設けた出口に
近く且つ落差がなるべく少ないことが好ましく、本実施
例では70mm程度の高度差となるように設定している。
Since the secondary steaming section C has the same structure as the primary steaming section A, the details of each section are omitted. However, in this secondary steaming section C, the soft rice grains that have not been cooked or are close to each other tend to stick to each other and easily harden, and the guide plate 27
Also, the second loosening machine 10b is attached to the front part, and preferably the middle part and the rear end, because the feed resistance becomes large and the feed resistance becomes large.
Third and fourth loosening machines 10c and 10d are provided at the places to improve the feeding assisting function as well as the leveling action to make the deposited thickness of the loosening and rice grains uniform. These loosening machines 10b-
Three units of 10d are synchronously driven via a chain. Further, the height of the mesh belt conveyor 8 is close to the outlet provided with the rear end guide piece 6c of the heated water tank 6 in order to prevent the rice 3 having a high water content coming out of the heated water tank 6 from being crushed by the impact of the drop. In addition, it is preferable that the head difference be as small as possible, and in this embodiment, the height difference is set to about 70 mm.

【0044】以上の如き構成の連続式炊飯装置1による
炊飯例を次に述べる。すなわち、一次蒸し部Aにおける
水蒸気温度を98〜102℃、水蒸気通過圧力を0.1
5kgH2 O /cm2 、送り時間を10分、二次浸漬部Bに
おける加熱水槽6中の水温を85〜90℃、浸漬時間を
6分、二次蒸し部Cにおける水蒸気温温度および通過圧
力を一次蒸し部Aと同一、送り時間を12分と設定した
際、ホッパー2より供給される一次浸漬処理を施した米
3は、一次蒸し部のメッシュベルトコンベヤ4にて移送
される過程でα化と糊化が進み含水率34%程度となっ
て第1のほぐし機10aにてほぐされると共に均一にな
らされ、スクレーパ15aおよびシュート16を通って
二次浸漬部Bの加熱水槽6に入る。ここでスクレーパコ
ンベヤ7の各スクレーパ板12の間に挟まれて移送さ
れ、α化の進行と共に均一に吸水膨潤されて表層部が柔
らかくなり、これにともない米粒から滲出するデンプン
溶液が水分中で糊化し、この糊化デンプンとともに水切
り兼用デンプン糊化液吸収用傾斜面6bに移送される。
An example of rice cooked by the continuous rice cooker 1 having the above structure will be described below. That is, the steam temperature in the primary steaming section A is 98 to 102 ° C., and the steam passing pressure is 0.1.
5 kg H 2 O / cm 2 , feed time 10 minutes, water temperature in the heating water tank 6 in the secondary immersion section B is 85 to 90 ° C., immersion time is 6 minutes, steam temperature temperature in the secondary steaming section C and passing pressure are When the feeding time is set to 12 minutes, which is the same as that in the primary steaming section A, the rice 3 that has been subjected to the primary dipping treatment supplied from the hopper 2 is converted into α in the process of being transferred by the mesh belt conveyor 4 in the primary steaming section. The gelatinization progresses to a water content of about 34%, which is loosened and evened by the first loosening machine 10a, and then passes through the scraper 15a and the chute 16 and enters the heating water tank 6 of the secondary dipping section B. Here, it is sandwiched between the scraper plates 12 of the scraper conveyor 7 and transferred, and as the gelatinization progresses, it is uniformly absorbed and swelled to soften the surface layer portion. As a result, the starch solution exuding from the rice grains is glued in water. The gelatinized starch is transferred to the slanted surface 6b for absorbing the gelatinized liquid of the starch, which also serves as a drainer.

【0045】図8は、米粒群3が上記傾斜面6b上をス
クレーパ板12によって移送される途上を拡大して示す
もので、米粒群3の内部には未だデンプン糊化液aが米
粒群3に吸収されない状態で含有していると共に、米粒
群3の上面にはスクレーパ板12によってすくい上げら
れた大量の不要なデンプン糊化液bが滞留している。
FIG. 8 is an enlarged view showing the way the rice grain group 3 is transferred on the inclined surface 6b by the scraper plate 12. Inside the rice grain group 3, the starch gelatinizing liquid a is still contained in the rice grain group 3. In addition to being contained in the rice grain group 3, a large amount of unnecessary starch gelatinization liquid b picked up by the scraper plate 12 remains on the upper surface of the rice grain group 3.

【0046】このような状態から米粒群3が徐々に上方
に移行する間に、不要な多量の水分の含んだデンプン糊
化液bは側方より二次浸漬部に還流され、また米粒群3
内に含有するデンプン糊化液aは、その移行途上で米粒
の芯内部まで十分に吸収され、含水率58〜63%程度
の半炊き状態で加熱水槽6の後端のガイド片6cから二
次蒸し部Cのメッシュベルトコンベヤ8上に移送され
る。
While the rice grain group 3 gradually moves upward from such a state, the starch gelatinization liquid b containing an unnecessary large amount of water is refluxed from the side to the secondary dipping section, and the rice grain group 3
The starch gelatinization liquid a contained therein is sufficiently absorbed inside the core of the rice grain during its transfer, and is secondary from the guide piece 6c at the rear end of the heating water tank 6 in a half-cooked state with a water content of 58 to 63%. It is transferred onto the mesh belt conveyor 8 in the steaming section C.

【0047】また上記傾斜面6bに沿って設けられるス
クレーパコンベヤ7は該傾斜面6bの延長線上におい
て、米粒3がガイド板6cに沿って二次蒸し部Cに移送
された直後に反転するようになっているため米粒3がス
クレーパ板12にすくい取られることはない。次いでメ
ッシュベルトコンベヤ8上の米粒3は第2〜第4のほぐ
し機10b〜10dによってほぐされ、且つ堆積厚が均
一になるようならされつつ蒸され、最終的に含水率63
〜65%程度、移送初期に比較した体積2.0倍程度
(ホッパー5内での体積に比較して2.7倍程度)のα
化と糊化が完成した完全な炊き上がり状態となってスク
レーパ15bより取出し部9から取出される。尚、取出
し部9では適当な受槽を置いたり、あるいは加工部等に
送る移送装置を設置すればよい。また炊飯の各種条件は
例示以外に種々変更できる。更に炊飯量は装置規模によ
って大きく異なり、制限はない。
Further, the scraper conveyor 7 provided along the inclined surface 6b is turned over immediately after the rice grains 3 are transferred to the secondary steaming section C along the guide plate 6c on the extension line of the inclined surface 6b. Therefore, the rice grains 3 are not scooped up by the scraper plate 12. Next, the rice grains 3 on the mesh belt conveyor 8 are steamed while being loosened by the second to fourth loosening machines 10b to 10d and being made to have a uniform deposition thickness, and finally the water content 63
About 65%, about 2.0 times the volume compared to the initial stage of transfer (about 2.7 times the volume in the hopper 5) α
It is in a completely cooked state in which the liquefaction and gelatinization have been completed, and it is taken out from the take-out section 9 from the scraper 15b. In the take-out section 9, an appropriate receiving tank may be placed, or a transfer device for sending to the processing section or the like may be installed. Further, various conditions for cooking rice can be variously changed other than the example. Furthermore, the amount of cooked rice varies greatly depending on the scale of the device, and there is no limit.

【0048】上記実施例ではホッパー2から一次浸漬処
理した米3を供給する構成としたが、一次蒸し部の前に
一次浸漬を連続的に行う設備を設け、原料米より一貫し
た連続式炊飯装置としてもよい。
In the above embodiment, the rice 3 which has been subjected to the primary soaking treatment is supplied from the hopper 2. However, a facility for continuously performing the primary soaking is provided before the primary steaming section, and a continuous type rice cooker that is more consistent with the raw rice. May be

【0049】[0049]

【効果】以上のように請求項1記載の発明によれば、特
に一次蒸し部と二次蒸し部とにおいて、両蒸し部を通過
する米粒群に対して均等に蒸気を送り込むことができ、
これによって蒸しムラのない均一な状態に蒸煮すること
ができ、これによって大量の製品を連続して製造するこ
とができるにもかかわらず、硬さ、粘り及び弾力性の3
要素のバランスのとれた食味(旨み)の良い米飯に仕上
げることができる。
As described above, according to the invention described in claim 1, particularly in the primary steaming section and the secondary steaming section, it is possible to evenly send steam to the rice grain groups passing through both steaming sections,
As a result, it can be steamed in a uniform state without unevenness of steaming, and although a large amount of products can be continuously produced, the hardness, tenacity and elasticity are 3
It is possible to finish cooked rice with a well-balanced element and good taste.

【0050】しかも蒸煮ムラや芯の残らないα化の完全
な良質の製品を得ることができる。
Moreover, it is possible to obtain a product of good quality which is completely free from unevenness of steaming and does not leave a core.

【0051】また本発明によれば、上記両蒸し部におい
て、加熱エネルギーの熱損失を最小限に止めて効率的に
蒸煮することができる。
Further, according to the present invention , in both of the steaming sections, the heat loss of the heating energy can be minimized and the steaming can be efficiently performed.

【図面の簡単な説明】[Brief description of drawings]

【図1】 この発明に係る連続式炊飯装置の実施例を示
すものであって、その装置全体の概略縦断面図、
FIG. 1 shows an embodiment of a continuous type rice cooking device according to the present invention, and is a schematic vertical sectional view of the entire device,

【図2】 同ホッパー部分の縦断面図である。FIG. 2 is a vertical sectional view of the hopper portion.

【図3】 図1のIII −III 線の断面矢視図である。3 is a cross-sectional view taken along the line III-III of FIG.

【図4】 同図3のIV−IV線の断面矢視図である。4 is a cross-sectional view taken along the line IV-IV of FIG.

【図5】 図1のV−V線の断面矢視図である。5 is a cross-sectional arrow view taken along line VV of FIG.

【図6】 図1のVI−VI線の断面矢視図である。6 is a cross-sectional view taken along the line VI-VI of FIG.

【図7】 図6のVII − VII線の断面矢視図である。FIG. 7 is a sectional view taken along line VII-VII of FIG.

【図8】 同要部の拡大説明図である。FIG. 8 is an enlarged explanatory diagram of the main part.

【図9】 従来例の要部縦断面図である。FIG. 9 is a longitudinal sectional view of a main part of a conventional example.

【符号の説明】[Explanation of symbols]

A 一次蒸し部 B 二次浸漬部 C 二次蒸し部 1 連続式炊飯装置 2 ホッパー(供給部) 2a 出口 3 米 4 メッシュベルトコンベヤ 4a メッシュベルト 5,5a 蒸気管 6 加熱水槽 6b 水切り兼用デンプン糊化液吸収用傾斜面 7 スクレーパコンベヤ 7d スクレーパコンベヤの終端部 8 メッシュベルトコンベヤ 8a メッシュベルト 9 取出し部 10a〜10d 第1〜第4のほぐし機 11 シャワー 12 スクレーパ板 19 シャッター 22a 開口 23 蒸気室 23a 蒸気室の底面 25 吹出し口 26 排水管 A Primary steaming part B Secondary dipping part C Secondary steaming part 1 Continuous rice cooker 2 Hopper (supply part) 2a Exit 3 Rice 4 Mesh belt conveyor 4a Mesh belt 5,5a Steam pipe 6 Heating water tank 6b Draining starch gelatinization Liquid absorption inclined surface 7 Scraper conveyor 7d Scraper conveyor end part 8 Mesh belt conveyor 8a Mesh belt 9 Extraction part 10a to 10d First to fourth disentangling machine 11 Shower 12 Scraper plate 19 Shutter 22a Opening 23 Steam room 23a Steam room Bottom 25 outlets 26 drainage pipes

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 水中浸漬処理を施した米の供給部と、供
給される米を移送するメッシュベルトコンベヤならびに
移送中の米を蒸す加熱水蒸気の吹出し口を備えた一次蒸
し部と、この蒸し部から連続的に供給される米を浸漬す
る加熱水槽ならびに該加熱水槽中の米を移送するスクレ
ーパコンベヤを備えた二次浸漬部と、この浸漬部から連
続的に供給される米を取出し部まで移送するメッシュベ
ルトコンベヤならびに移送中の米を蒸す加熱水蒸気の吹
出し口とを備えた二次蒸し部とを有してなる連続式炊飯
装置において、前記一次蒸し部と前記二次蒸し部とには
それぞれ上方が前記メッシュベルトコンベヤに面して開
しコンベヤの移動方向に分割された複数の蒸気室が設
けられ、各蒸気室に上記コンベヤの移動方向に直交する
蒸気室幅方向全域にわたって蒸気管が配設されると共
に、各蒸気管には蒸気吹き出し口が下向きに穿設され、
前記複数の蒸気室は各底面の幅方向片側が低くなるよう
に傾斜し、且つ各蒸気室は上記底面の低位側において互
いに連通して排水管に連結されてなる連続式炊飯装置。
1. A primary steaming section provided with a submerged rice supply section, a mesh belt conveyor for transferring the supplied rice, and an outlet for heated steam for steaming the transferred rice, and this steaming section. From a dipping section equipped with a heating water tank for immersing rice continuously supplied from the above and a scraper conveyor for transferring the rice in the heating water tank, and transferring rice continuously supplied from this dipping section to a unloading section In a continuous rice cooker having a mesh belt conveyor and a secondary steaming section provided with an outlet for heating steam for steaming rice being transferred, the primary steaming section and the secondary steaming section respectively have A plurality of steam chambers are provided, the upper part of which faces the mesh belt conveyor and is divided in the conveyor moving direction.
And is orthogonal to the moving direction of the above conveyor in each steam chamber
When the steam pipes are installed over the entire width of the steam chamber,
In addition, each steam pipe is provided with a steam outlet downward,
In the plurality of steam chambers, one side of each bottom in the width direction should be low.
And the steam chambers are mutually connected on the lower side of the bottom surface.
A continuous rice cooker that is connected to the sea urchin and connected to the drain pipe .
JP5214591A 1993-08-01 1993-08-30 Continuous rice cooker Expired - Fee Related JPH07108260B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5214591A JPH07108260B2 (en) 1993-08-01 1993-08-30 Continuous rice cooker

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5214591A JPH07108260B2 (en) 1993-08-01 1993-08-30 Continuous rice cooker

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP62147311A Division JPS6328360A (en) 1987-06-13 1987-06-13 Continuous rice boiling device

Publications (2)

Publication Number Publication Date
JPH06181842A JPH06181842A (en) 1994-07-05
JPH07108260B2 true JPH07108260B2 (en) 1995-11-22

Family

ID=16658259

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5214591A Expired - Fee Related JPH07108260B2 (en) 1993-08-01 1993-08-30 Continuous rice cooker

Country Status (1)

Country Link
JP (1) JPH07108260B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1156631A (en) * 1997-08-25 1999-03-02 Fujimori Kogyo Kk Steaming device
JP5519980B2 (en) * 2009-09-15 2014-06-11 株式会社テイエルブイ Steam heating device
JP5525788B2 (en) * 2009-09-15 2014-06-18 株式会社テイエルブイ Steam heating device
WO2011111231A1 (en) * 2010-03-12 2011-09-15 埼玉県 Heat food preparation device and heat food preparation method
CN115843956A (en) * 2022-11-16 2023-03-28 武汉中百古唐美膳中央厨房有限责任公司 Continuous steam rice production line

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5724111B2 (en) * 1974-05-13 1982-05-22
JPS6012945A (en) * 1983-07-05 1985-01-23 Horiken Kogyo Kk Continuous treatment of grain and device therefor

Also Published As

Publication number Publication date
JPH06181842A (en) 1994-07-05

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