JPH0469982B2 - - Google Patents

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Publication number
JPH0469982B2
JPH0469982B2 JP62147311A JP14731187A JPH0469982B2 JP H0469982 B2 JPH0469982 B2 JP H0469982B2 JP 62147311 A JP62147311 A JP 62147311A JP 14731187 A JP14731187 A JP 14731187A JP H0469982 B2 JPH0469982 B2 JP H0469982B2
Authority
JP
Japan
Prior art keywords
rice
section
steaming
rice grains
water tank
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 - Lifetime
Application number
JP62147311A
Other languages
Japanese (ja)
Other versions
JPS6328360A (en
Inventor
Yoshihiro Koresawa
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.)
KORESAWA TETSUKOSHO KK
Original Assignee
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 KORESAWA TETSUKOSHO KK filed Critical KORESAWA TETSUKOSHO KK
Priority to JP62147311A priority Critical patent/JPS6328360A/en
Publication of JPS6328360A publication Critical patent/JPS6328360A/en
Publication of JPH0469982B2 publication Critical patent/JPH0469982B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 (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。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a continuous rice cooking device that is suitably used in fields where large quantities of rice are cooked, such as in the lunch box catering industry, food service companies, and restaurant industries.

(従来技術) 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。
(Prior Art) The latest conventional technology of this type of continuous rice cooking apparatus is disclosed in Japanese Patent Application Laid-Open No. 12945/1983.

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 device includes a primary steaming section where the rice grains soaked in water are steamed while being transferred by a belt conveyor, and a secondary soaking section where the rice grains fed from the primary steaming section are immersed in water while being sequentially transferred by a scraper conveyor. It is equipped with a secondary steaming section where the rice grains soaked in the secondary soaking section are further transferred by a belt conveyor and subjected to secondary steaming.

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。
This latest conventional technology has the advantage of being able to continuously cook a large amount of rice at once, but has the disadvantage that the taste (umami) of the cooked rice is inferior.

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。
Although it is important for this type of rice cooking device to efficiently handle large quantities of rice, the most important thing is how to improve the taste of the cooked rice. Even if a large amount of rice can be processed, it will be of no use if the rice tastes bad.

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 better understand the present invention, the theory regarding the taste of cooked rice will be explained first, and then the characteristics of the present invention will be described.

米飯の食味(これをテクスチヤー、texture)
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
保つ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 rice (texture)
It is said that food quality lies in the balance of three elements: hardness, stickiness, and elasticity. In particular, the taste (umami) of rice is overwhelmingly related to hardness and stickiness, and it is important that the two of them are kept in balance with each other. Absolutely necessary. Even if the rice is a little hard, if it has a stickiness proportional to the hardness, it can be said to be delicious.If the same hard rice is not sticky enough, the balance has been disrupted and the rice is not delicious. to go into.

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。
In order to maintain a good balance of the above three elements in cooked rice, it is necessary to consider the time for soaking the rice in water, the amount of water added, and the method and time of steaming.

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 above-mentioned soaking process, the cooked rice absorbs water and swells, and the starchy components containing dextrin, free amino acids, and free sugars that improve the taste of the cooked rice are eluted and become a gelatinized liquid, which is absorbed into the cooked rice. However, if more water is absorbed than necessary during this soaking process, the hardness of the cooked rice, which is the most important element for taste, will be lost.

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 soaking process, if the amount of water absorbed in the final process (steaming process) to achieve the best taste is 100%, the amount of water absorbed is limited to 85 to 90%, and the hardness of the cooked rice is maintained. There is a need to.

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 mentioned above, the starchy gelatinizing liquid is absorbed into the rice grains during the soaking process, but if more moisture is absorbed than necessary at this time, the rice grains will lose their hardness.

したがつ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 soaking process, the starch gelatinizing liquid must be sufficiently absorbed into the rice grains, but the rice grains must be formed in a structure that does not absorb more water than necessary.

しかもこのデンプン質糊化液が米粒に吸収され
ることによつて後続の蒸らし工程で十分に混練す
ることによつて十分な粘りを生ぜしめることにな
る。
In addition, this starchy gelatinizing liquid is absorbed into the rice grains and sufficiently kneaded in the subsequent steaming step, resulting in sufficient viscosity.

即ち、二次蒸し部ではほぐし機によつて米粒を
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つた。
That is, in the secondary steaming section, it is necessary to sufficiently knead the rice grains using a loosening machine to create stickiness among the rice grains, but conventional equipment does not take this into account, resulting in an even worse taste.

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 addition, during the soaking process (secondary soaking part), it is necessary for the rice grains to sufficiently absorb the starchy gelatinizing liquid, which has the greatest effect on taste and stickiness; The hardness of the rice grains, which is a key element, will be lost.

したがつ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つて米飯
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
いつても過言ではない。
Therefore, in this soaking process, the taste of the rice will be greatly affected depending on how the above-mentioned contradictory propositions are rationally resolved, and the success or failure of this type of rice cooking device lies in the treatment of this soaking process. It is no exaggeration to say that.

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、不完全であつたため食味
の良い米飯を製造することができなかつた。
In the conventional apparatus, the processing especially in this dipping step (secondary dipping section) was insufficient and incomplete, making it impossible to produce cooked rice with good taste.

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、第9図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に沿つてスクレーパコンベヤ4
1がプーリ42によつて懸架されている。加熱水
槽40の終端部底壁40aはスクレーパコンベヤ
41の回動軌跡に沿つ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41によつて次の二次蒸し部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 parts of the prior art described above will be explained with reference to the drawings. FIG. 9 shows the terminal end of the secondary immersion section 39 of the prior art, 40 is a heating water tank,
A scraper conveyor 4 is installed along this heating water tank 40.
1 is suspended by a pulley 42. The bottom wall 40a of the end portion of the heating water tank 40 is formed in an arc shape along the rotation locus of the scraper conveyor 41, and is filled with heated water 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, gelatinization and water absorption swelling progress during the transfer, and at the end, the rice grains 3 are sent to the next secondary steaming section 43 by the scraper conveyor 41. However, in this conventional technology, when the rice grains 3 in the heating water tank 40 are pressed by the scraper conveyor 41 and are transferred over the upper edge 40b of the terminal end, the rice grains 3 remain in a large amount of moisture because there is no drainage section. will be transferred.

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
のメツシユ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つた。
For this reason, the rice grains absorb more water than necessary in the secondary soaking section, causing them to lose their hardness.Furthermore, the rice grains are transferred to the secondary steaming section with a large amount of moisture, so the rice grains are not water-added in the secondary steaming section. At the same time, a large amount of water falls down from the mesh of the belt conveyor in the secondary steaming section, and the starch gelatinizing components attached to the rice grains are washed away. As a result, the rice grains lose their stickiness.
There was a problem that made the taste even worse.

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つた。
Further, in the conventional apparatus described above, since the transfer state is uneven, there is a problem that uneven water absorption occurs in the secondary immersion section and uneven steaming occurs in the secondary steaming section, resulting in incomplete steaming.

即ち予め水中浸漬処理された米粒を一次蒸し部
によつて一次蒸しすることによつて米はある程度
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つている。したが
つ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
の塊となつ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, by first steaming rice grains that have been soaked in water in advance in the primary steaming section, the rice undergoes gelatinization and gelatinization to a certain extent, and the rice grains become stuck together, leaving the rice grains in a half-clump state at the end of the primary steaming section. It's getting old. Therefore, if the rice grains are fed into the next secondary dipping section in this state as in the conventional device described above, the lumps of rice grains will continue to be transferred to the secondary dipping section intermittently as large and small lumps. Not only will the rice grains not be sent in fixed amounts to the secondary soaking section, but the rice grains will be transported in the form of lumps, so the rice grains in the center of the lumps will not be able to have a sufficient water absorption effect.

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つて二次蒸し部のベ
ルトコンベヤに堆積される米粒の堆積厚が移送方
向に凹凸状となつ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、これによつて
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
つ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つてい
た。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つ
た。
In addition, when the rice grains that have been soaked in the secondary soaking section and have undergone further gelatinization and water absorption swelling are pressed and transferred to the scraper conveyor, at the end of the secondary soaking section, a large number of gelatinized rice grains are transferred to the conveyor in the form of lumps. However, in the conventional device described above, the rice grains are sent in this state to the next secondary steaming section, so the amount of rice grains fed becomes even more intermittent, causing them to accumulate on the belt conveyor of the secondary steaming section. The thickness of rice grains deposited on the scraper conveyor becomes uneven in the transport direction, which causes uneven steam passage and causes uneven steaming.At the same time, rice lumps adhering to the scraper conveyor are returned to the secondary soaking section. As a result, the moisture in the secondary immersion part turns into a turbid paste liquid, and this pasty turbid liquid adheres to the surface of the rice grains in the form of a film, and this film further enhances the water absorption effect. This causes uneven water absorption, and water is not absorbed to the core of the rice grain, so even after passing through the secondary steaming section, the core is not sufficiently gelatinized, resulting in a grainy finish with a rough texture. As described above, in the above-mentioned conventional apparatus, the steamed rice was incomplete and a product of good quality could not be obtained.

(発明が解決しようとする問題点) 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つて、
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。
(Problems to be Solved by the Invention) This invention provides a continuous rice cooker of this type that
By faithfully practicing the rice cooking theory mentioned above,
The purpose is to eliminate uneven water absorption and uneven steaming to produce uniform, high-quality cooked rice with good taste (umami).

(問題点を解決するための手段) 上記問題点を解決するために、この発明は、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、二次浸漬部の加熱水槽終端部に、該水
面より斜め上方に延びる水切り兼用デンプン糊化
液吸収用傾斜面が設けられると共に、二次浸漬部
に備えるスクレーパコンベヤは前記傾斜面に沿つ
て配設され、更に一次蒸し部及び二次蒸し部の各
ベルトコンベヤに対して各ベルトコンベヤの送り
速度よりも速く回転する第1及び第2のほぐし機
がそれぞれ設けられてなる構成を採用するもので
ある。
(Means for Solving the Problems) In order to solve the above problems, the present invention provides a supply section for rice soaked in water, a belt conveyor for transporting the supplied rice, and a belt conveyor for transporting the rice during transport. A primary steaming section equipped with an outlet for steaming heated steam, a heated water tank in which the rice continuously supplied from the steaming section is immersed, and a secondary immersion section equipped with a scraper conveyor for transferring the rice in the heated water tank. , a secondary steaming section equipped with a belt conveyor that transfers the rice continuously supplied from the soaking section to the take-out section and a heated steam outlet for steaming the rice being transferred; At the end of the heating water tank, a sloped surface for absorbing the starch gelatinizing liquid that also serves as a drainer is provided and extends obliquely upward from the water surface, and a scraper conveyor provided in the secondary immersion section is disposed along the slope, and further A configuration is adopted in which first and second loosening machines are provided for each of the belt conveyors in the steaming section and the secondary steaming section, respectively, which rotate faster than the feed speed of each belt conveyor.

(作用) 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つて順次
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化と糊化が進行し米粒間が付着し
て半塊状態になつているが一次蒸し部終端位置に
は、ベルトコンベヤの送り速度より順方向に速く
回転する第1のほぐし機が設けられているため、
このほぐし機によつて半塊状態の米粒が効率よく
ほぐされ、且つならされた状態で次の二次浸漬部
に送り込まれることになり、これがため米粒が定
量宛連続的に送り込まれる。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水切り
兼用デンプン糊化液吸収用傾斜面に移送される。
(Function) The rice grains supplied from the water-soaked rice supply section to the primary steaming section are sequentially and continuously transported by a belt conveyor, and by the time they reach the end of the primary steaming section, the rice grains have undergone gelatinization and gelatinization to some extent. As the rice progresses, the grains of rice stick together and become half-clumps, but at the end of the primary steaming section there is a first loosening machine that rotates faster than the feed speed of the belt conveyor.
This loosening machine efficiently loosens the half-clumped rice grains and sends them in a flattened state to the next secondary soaking section, so that the rice grains are continuously fed into a fixed amount. In the secondary immersion section, the rice grains are pressed by a scraper conveyor and transferred one after another, and during the transfer, water is uniformly absorbed into the rice grains, and in a state where gelatinization and water absorption swelling have progressed, rice grains are released from the water surface at the end of the secondary immersion section. The starch gelatinizing liquid is transferred to an upwardly extending inclined surface that also functions as a drainer and absorbs the starch gelatinizing liquid.

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 moisture that is sent along with the rice grains while being gradually transferred along the above-mentioned slope is returned to the secondary soaking section from the side, and the rice grains on the slope absorb more moisture than necessary. It is possible to maintain appropriate hardness without any problems.

したがつ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
用と相俟つて粘性と弾性を生ぜしめることにな
る。
Therefore, only the rice grain groups containing an appropriate amount of starch gelatinization liquid remain on the slope, and as these are gradually transferred, the starch gelatinization liquid is sufficiently absorbed by the rice grain groups to the inside of the core. This, together with the action of the next secondary steaming section, produces viscosity and elasticity.

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、これらの米粒が第2のほぐし機
によつ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つて
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。
In this way, unnecessary moisture is removed on the above slope,
The rice grains that have absorbed the necessary starch gelatinization liquid are transferred to the secondary steaming section, where these rice grains are loosened by a second loosening machine, and the starch cell membranes in the gelatinization liquid attached to the rice grains are partially destroyed. By fully kneading the starchy ingredients leached with dextrin, free amino acids, and free sugars that improve the taste, they give the rice grains stickiness and shine, which are important elements in terms of taste. It will end.

更に第2のほぐし機によつてほぐされることに
よつて米粒の体積が均一にならされ、従つて米粒
の堆積厚が移送方向に略一定厚になつて移送さ
れ、その移送途上における二次蒸気の米粒への通
過量が常に均一となり蒸しムラが発生することが
ない。
Furthermore, by being loosened by a second loosening machine, the volume of the rice grains is made uniform, so that the stacked rice grains are transferred with a substantially constant thickness in the transfer direction, and secondary steam is generated during the transfer. The amount of water that passes through the rice grains is always uniform, and uneven steaming does not occur.

(実施例) 以下、この発明を図示実施例に基づいて説明す
る。
(Embodiments) The present invention will be described below based on illustrated embodiments.

第1図で示すように、連続式炊飯装置1は、ホ
ツパー2より供給される一次浸漬処理を施した米
粒3をメツシユベルトコンベヤ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つて
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と同様にメツシユベルトコンベヤ
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つて移す二次蒸し部
Cとから構成されている。そして一次蒸し部Aに
おけるメツシユベルトコンベヤ4の後端に第1の
ほぐし機10aが、二次蒸し部Cにおけるメツシ
ユベルトコンベヤ8の前部に第2のほぐし機10
b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ヤワー、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、15aはメツシユベルトコンベヤ
4の後端においてメツシユベルト4aに摺接して
米粒をシユート16に落下させるスクレーバ、1
5bはメツシユベルトコンベヤ8の後端において
メツシユベルト8aに摺接した炊き上がつた米を
取出し部9へ案内するスクレーパ、17aはメツ
シユベルトコンベヤ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,10c,10dとを
それぞれ別個の可変速モータで駆動してもよいこ
とは勿論である。17cはメツシユベルトコンベ
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に接触してシヤ
ワー11を間歇作動させるリミツトスイツチであ
る。
As shown in FIG. 1, the continuous rice cooking device 1 includes heated steam blown out from a steam pipe 5 while transporting rice grains 3 that have been subjected to primary soaking treatment supplied from a hopper 2 at a constant speed on a mesh belt conveyor 4. a primary steaming section A in which the rice grains 3 continuously supplied from the steaming section A are immersed in a heated water tank 6 and transferred by a scraper conveyor 7;
The rice grains 3 are continuously supplied from this soaking section B.
Similarly to the primary steaming section A, the steam pipe 5
It consists of a secondary steaming section C in which the steam is transferred by heated steam blown out from the steaming section C. A first loosening machine 10a is installed at the rear end of the mesh belt conveyor 4 in the primary steaming section A, and a second loosening machine 10a is installed at the front of the mesh belt conveyor 8 in the secondary steaming section C.
Similarly, third and fourth loosening machines 10c and 10d are attached to the middle part and rear end of the machine b. 11 is a shower that injects heated water to clean the scraper plate 12 of the scraper conveyor 7 at a position where it is separated from the heating water tank 6; 13 is a temperature sensor that measures the water temperature in the heating water tank 6; and 14 is a drain of the heating water tank 6. , 15a is a scraper 1 which slides on the mesh belt 4a at the rear end of the mesh belt conveyor 4 and drops the rice grains into the chute 16;
5b is a scraper that guides the cooked rice that is in sliding contact with the mesh belt 8a at the rear end of the mesh belt conveyor 8 to the take-out section 9; 17a is a variable speed motor that drives the mesh belt conveyor 4; 17b is the scraper conveyor 7 This is a variable speed motor that drives three loosening machines 10b, 10c, and 10d in the secondary steaming section C. It goes without saying that the conveyor 7 and the loosening machines 10b, 10c, and 10d may be driven by separate variable speed motors. 17c is a variable speed motor that drives the mesh belt conveyor 8, and 18 is a limit switch that contacts a cam 18a that is interlocked with the variable speed motor 17b to operate the shower 11 intermittently.

ホツパー2は、第2図で示すように、蓋板2a
のフランジ状縁部に上端に固着したハンドル19
aにて回転するねじ軸19が垂設されており、こ
のねじ軸19に螺合した昇降子19bに固着され
た板状シヤツター20をガイド板20aに沿つて
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の開口幅とメツシユベ
ルトコンベヤ4の送り速度とを調整することによ
つて米3の供給量が広範囲で調整できる。
As shown in FIG. 2, the hopper 2 has a lid plate 2a.
a handle 19 fixed at the upper end to the flanged edge of the
A screw shaft 19 that rotates at a point a is vertically installed, and by sliding a plate-shaped shutter 20 fixed to an elevator 19b screwed onto the screw shaft 19 up and down along a guide plate 20a, the exit opening is opened. The vertical opening width of 2a can be adjusted as desired.
That is, by adjusting the opening width of the outlet opening 2a and the feeding speed of the mesh belt conveyor 4, the amount of rice 3 supplied can be adjusted over a wide range.

一次蒸し部Aにおいて、メツシユベルトコンベ
ヤ4のメツシユベルト4aは目の細かいステンレ
ス製ネツトなどから形成されており、第3図およ
び第4図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
から移送方向に沿つ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〓
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
加熱水蒸気がメツシユベルト4aを通して、両側
ガイド板24,24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。
尚、各吹出し口25が下向きに開口しているの
は、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。尚、蒸気室23の底面は片
側が低くなるように傾斜し、かつ複数の蒸気室2
3,23……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 made of fine stainless steel net, and as shown in FIGS. Casing plate 21 opened upward on the side
A plurality of steam chambers 23 are constituted by the steam chambers 23 and the partition plates 22, 22, . In addition, vertical guide plates 2 are provided on both side flange portions 21a and 21a of the casing plate 21, respectively.
4 is fixed at its lower flange portion 24a, and both end edges of the upper belt 4a have a slight gap between the flange portions 21a and 24a.
It is arranged so that it is sandwiched in between. Each branch pipe 5a of the steam pipe 5 is arranged to protrude horizontally into each steam chamber 23, and the heated steam ejected from downward outlet ports 25 bored at predetermined intervals in the branch pipe 5a passes through the mesh belt 4a. The rice 3 is blown into the accumulated layer of rice 3 that is being transferred between the guide plates 24 and 24 on both sides, and a steaming action is performed.
The reason why each outlet 25 opens downward is to allow the heated steam to fill the steam chamber 23 once and be blown into the deposited layer evenly from the entire upper surface of the steam chamber 23, thereby preventing localized steaming. This is to prevent excess or deficiency from occurring. The bottom surface of the steam chamber 23 is sloped so that one side is lower, and a plurality of steam chambers 2
3, 23... communicate through openings 22a provided in the partition plate 23 on the lower side of the slope, and the water condensed in each steam chamber 23 is collected on the lower side of the slope and discharged from the drain pipe 26. It is made to be done. 27 is a mounting frame made of angle material or the like.

一方、第1〜第4のほぐし装置10a〜10d
は、第5図で示すように、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2
9の回転に伴つて各ピン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
がメツシユベルト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29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3
0,31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はメツシユベルトコンベヤ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 10d
As shown in FIG.
Cylindrical rotating shafts 29 are installed radially in the axial direction at regular intervals and at different angles, and are installed horizontally between a drive support shaft 30 and a pivot shaft 31.
As the rice grains 9 rotate, each pin 28 sequentially enters the deposited layer of rice grains 3 to loosen and smooth the rice grains. This rotation is normally carried out by conveyor 4,
8, and the moving speed of the tip of the pin 28 is set to be faster than the feeding speed of the mesh belts 4a, 8a, preferably about 3 times,
As a result, in addition to the above-mentioned loosening and leveling effects, an assisting effect for feeding the rice grains 3 is exerted. In addition, since the pin 28 needs to be periodically cleaned and removed from rice cakes that accumulate during operation, the rotating shaft 29 has a split groove 29a at one end that engages with the locking pin 30a of the drive support shaft 30.
Both support shafts 3
It has a structure that allows it to be easily attached and detached from the 0.0 and 31. 30b is a bearing of the drive shaft 30, 31b is a bearing of the pivot shaft 31, and 32 is a mesh belt conveyor 8.
This is the mounting plate for the drive pulley.

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6
c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
になつている。そしてこの加熱水槽6内には、第
6図に示すように、シユート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34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つてい
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7a,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条の無端チエーン7d,7dが巻き掛け
られ、したがつて該コンベヤ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6
bに沿つて設けられ、その延長線上で反転するよ
うになつている。第7図でも示すようにこれらチ
エーン7d,7d間にわたつて所定間隔毎にL字
状取付片12aを介してスクレーパ板12がチエ
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、下側チエーン位置でガイド
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〓をもつ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 section B, the heating water tank 6 consists of a horizontal surface 6a extending from the front to the center, an upwardly inclined surface 6b at the rear continuous to this, and a guide surface 6c rapidly hanging down from the inclined surface. 6b has an inclination of approximately 20 to 40 degrees as shown, and the guide surface 6
c is formed with an inclination of 50 to 70 degrees between it and the inclined surface 6b, and furthermore, the inclined surface 6b extends higher than the water surface of the water 33 in the heating water tank 6, and the inclined surface 6b has a slope of 50 to 70 degrees. It also functions as a starch gelatinizing liquid absorption process in which the starch gelatinizing liquid contained within the colander and the rice grains is absorbed into the core of the rice grains. In this heating water tank 6, as shown in FIG. 6, a guide frame 34 is disposed with an upwardly open U-shaped cross section continuous from the chute 16, with the bottom surface in close contact with the horizontal part 6a and the inclined part 6b. A heating steam pipe 35 is disposed in the water 33 so as to surround the outside of the guide frame 34, and as is clear from the diagram, the outer chamber and the inner chamber with the guide frame 34 in between are disposed in the water 33. Heated water is configured to circulate between the chamber and the chamber in which the rice grain groups are accommodated. On the other hand, the scraper conveyor 7 has a heating water tank 6
Two parallel endless chains 7d, 7d are connected to each pair of driven pulleys 7a, 7b arranged at the same height on the horizontal plane 6a, and to the driving pulley 7c arranged at a high position on the extension line of the rear end of the draining slope 6b. wrapped around and thus the terminal lower surface 7d of the conveyor 7
is the inclined surface 6 for absorbing the starch gelatinizing liquid which also serves as a drainer.
b, and is designed to be reversed on its extension line. As shown in FIG. 7, scraper plates 12 are mounted at predetermined intervals between the chains 7d, 7d via L-shaped mounting pieces 12a at right angles to the chain direction. Each scraper plate 12 is set to pass through the guide frame 34 at the lower chain position with both side ends and the lower end leaving a space large enough to prevent rice grains from entering and exiting. In addition, a pulley 7e is attached to the rotating 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.

シヤワー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つた際に加熱水を噴
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
ツ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
ツトスイツチ18の信号を受けて上記1ピツチ毎
に一定時間だけ、例えば1ピツチ移動時間を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 close to the drive pulley 7c of the scraper conveyor 7, and sprays heated water when each scraper plate 12 detached from the heating water tank 6 assumes a fan-shaped open position at the position around the pulley 7c. Rice grains 3 attached to the surface of the scraper plate 12
It functions to wash off the water to the secondary steaming section C side together with the heated water. This injection is performed by setting the cam 18a to make one revolution for each pitch of movement of each scraper plate 12, and by receiving a signal from the limit switch 18 that contacts the cam 18a, for a certain period of time every pitch. For example, when one pitch movement time is one minute, the movement is performed for about 3 to 6 seconds.

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はチエーンを介して3基が同期駆動する。
またメツシユベルトコンベヤ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。
The secondary steaming section C has the same structure as the primary steaming section A, so details of each section will be omitted. However, in this secondary steaming section C, the rice grains are not completely cooked, and the soft rice grains in a similar state tend to stick to each other and harden, and also stick to the guide plate 27, increasing the feeding resistance, so the second loosening machine 10b is used. 3rd and 4th sections at the front and preferably at three locations in the middle and at the rear end.
The loosening machines 10c and 10d are provided to enhance the feeding function as well as the loosening and leveling action to make the accumulated thickness of rice grains uniform. These loosening machines 10b~
Three units 10d are driven synchronously via a chain.
In addition, the height of the mesh belt conveyor 8 is set so that the outlet has a guide piece 6c at the rear end of the heating water tank 6, in order to prevent rice 3 with a high moisture content coming out of the heating water tank 6 from being crushed by the impact of falling. It is preferable to be close to each other and have as little head difference as possible, and in this embodiment, the height difference is set to be about 70 mm.

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
0.15KgH2O/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、ホツパー2より供給される一
次浸漬処理を施した米3は、一次蒸し部のメツシ
ユベルトコンベヤ4にて移送される過程でα化と
糊化が進み含水率34%程度となつて第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およびシユート16を通つて二
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 cooking using the continuous rice cooking apparatus 1 having the above configuration will be described next. In other words, the steam temperature in primary steaming section A is 98 to 102℃, and the steam passing pressure is
0.15KgH 2 O/cm 2 , feeding time 10 minutes, secondary immersion part B
The water temperature in the heating water tank 6 is 85 to 90°C, the immersion time is 6 minutes, the steam temperature and passing pressure in the secondary steaming section C are the same as those in the primary steaming section A, and the feeding time is
When the setting is 12 minutes, the rice 3 that has been subjected to the primary soaking process and supplied from the hopper 2 undergoes gelatinization and gelatinization during the process of being transferred to the mesh belt conveyor 4 in the primary steaming section, resulting in a water content of 34%. It is loosened and smoothed uniformly by the first loosening machine 10a,
It enters the heating water tank 6 of the secondary immersion section B through the scraper 15a and the chute 16. Here, the rice is transferred between the scraper plates 12 of the scraper conveyor 7, and as gelatinization progresses, it uniformly absorbs water and swells, making the surface layer soft. The gelatinized starch is then transferred to the inclined surface 6b for draining and absorbing the starch gelatinization liquid.

第8図は、米粒群3が上記傾斜面6b上をスク
レーパ板12によつ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1
2によつ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 shows an enlarged view of the rice grain group 3 being transferred on the inclined surface 6b by the scraper plate 12, and the starch gelatinization liquid a is still inside the rice grain group 3. In addition, there is a scraper plate 1 on the top surface of the rice grain group 3.
A large amount of unnecessary starch gelatinization liquid b scooped up by step 2 remains.

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のメツシユベ
ルトコンベヤ8上に移送される。
While the rice grain group 3 gradually moves upward from this state, the starch gelatinizing solution b containing an unnecessary large amount of water is refluxed from the side to the secondary soaking part, and is also contained in the rice grain group 3. The starch gelatinizing liquid a is sufficiently absorbed into the core of the rice grains during the transition, and is passed from the guide piece 6c at the rear end of the heating water tank 6 to the secondary steaming section C in a half-cooked state with a water content of about 58 to 63%. is transferred onto a mesh belt conveyor 8.

また上記傾斜面6bに沿つ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に沿つて二次蒸し部C
に移送された直後に反転するようになつているた
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。次いでメツシユベルトコンベヤ8上の
米粒3は第2〜第4のほぐし機10b〜10dに
よつてほぐされ、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(ホツパ
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つてス
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つて大きく異な
り、制限はない。
Further, the scraper conveyor 7 provided along the slope 6b allows the rice grains 3 to be moved along the guide plate 6c to the secondary steaming section C on the extension line of the slope 6b.
Since the rice grains 3 are turned over immediately after being transferred to the scraper plate 12, 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 loosened by the second to fourth looseners 10b to 10d, and steamed while making the pile thickness uniform, and finally have a moisture content of 63 to 65. %, about 2.0 times the volume compared to the initial stage of transfer (about 2.7 times the volume in the hopper 5), and is in a completely cooked state where gelatinization and gelatinization have been completed. taken from.
Incidentally, in the take-out section 9, a suitable receiving tank may be placed, or a transfer device for sending the material to a processing section or the like may be installed.
Moreover, various conditions for rice cooking can be changed in various ways other than those shown in the examples. Furthermore, the amount of rice to be cooked varies greatly depending on the scale of the device, and there is no limit.

上記実施例ではホツパー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 that has been subjected to the primary soaking process is supplied from the hopper 2, but it is also possible to install equipment to continuously perform the primary soaking process in front of the primary steaming section to create a continuous rice cooking device that is more consistent than raw rice. .

(効果) この発明によれば、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。
(Effects) According to this invention, even though it is possible to continuously manufacture a large amount of products, it is possible to produce rice with good taste (umami) and a well-balanced balance of the three elements of hardness, stickiness, and elasticity. be able to.

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 completely gelatinized, high-quality product with no uneven steaming or core residue.

【図面の簡単な説明】[Brief explanation of the drawing]

図面はこの発明に係る連続式炊飯装置の実施例
を示すものであつて、第1図は装置全体の概略縦
断面図、第2図はホツパー部分の縦断面図、第3
図は第1図の−線の断面矢視図、第4図は第
3図の−線の断面矢視図、第5図は第1図の
−線の断面矢視図、第6図は第1図の−
線の断面矢視図、第7図は第6図の−線の断
面矢視図、第8図は本発明の要部の拡大説明図、
第9図は従来例の要部縦断面図である。 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……ホツ
パー(供給部)、2a……出口、3……米、4…
…メツシユベルトコンベヤ、4a……メツシユベ
ルト、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
……メツシユベルトコンベヤ、8a……メツシユ
ベルト、9……取出し部、10a〜10d……第
1〜第4のほぐし機、11……シヤワー、12…
…スクレーパ板、19……シヤツター、25……
吹出し口。
The drawings show an embodiment of the continuous rice cooking device according to the present invention, in which FIG. 1 is a schematic vertical cross-sectional view of the entire device, FIG. 2 is a vertical cross-sectional view of the hopper portion, and FIG.
The figure is a cross-sectional view taken along the - line in Figure 1, Figure 4 is a cross-sectional view taken along the - line in Figure 3, Figure 5 is a cross-sectional view taken along the - line in Figure 1, and Figure 6 is a cross-sectional view taken along the - line in Figure 1. Figure 1 -
7 is a cross-sectional view taken along the - line in FIG. 6, FIG. 8 is an enlarged explanatory view of the main parts of the present invention,
FIG. 9 is a vertical sectional view of the main part of the conventional example. A...Primary steaming section, B...Secondary soaking section, C...
Secondary steaming section, 1... Continuous rice cooker, 2... Hopper (supply section), 2a... Outlet, 3... Rice, 4...
...Mesh belt conveyor, 4a...Mesh belt, 6...Heating water tank, 6b...Slope for draining and absorbing starch gelatinizing liquid, 7...Scraper conveyor, 7d...Terminal part of scraper conveyor, 8
...Mesh belt conveyor, 8a...Mesh belt, 9...Take-out section, 10a to 10d...First to fourth loosening machines, 11...Shower, 12...
...Scraper plate, 19...Shutter, 25...
Air outlet.

Claims (1)

【特許請求の範囲】[Claims] 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、二次浸漬部の加熱水槽終端部
に、該水面より斜め上方に延びる水切り兼用デン
プン糊化液吸収用傾斜面が設けられると共に、二
次浸漬部に備えるスクレーパコンベヤは前記傾斜
面に沿つて配設され、更に一次蒸し部及び二次蒸
し部の各ベルトコンベヤに対して各ベルトコンベ
ヤの送り速度よりも速く回転する第1及び第2の
ほぐし機がそれぞれ設けられてなる連続式炊飯装
置。
1. A supply section for rice soaked in water, a primary steaming section equipped with a belt conveyor for transferring the supplied rice, a heated steam outlet for steaming the rice being transferred, and a continuous supply from this steaming section. A secondary dipping section equipped with a heated water tank in which the rice is immersed, a scraper conveyor that transfers the rice in the heated water tank, and a belt conveyor and transfer section that transfers the rice continuously supplied from this dipping section to a take-out section. It has a secondary steaming section equipped with a heated steam outlet for steaming the rice inside, and at the end of the heated water tank of the secondary soaking section, there is a slope for absorbing starch gelatinizing liquid that also serves as a drainer and extends obliquely upward from the water surface. A scraper conveyor provided in the secondary dipping section is disposed along the inclined surface, and the scraper conveyor provided in the secondary dipping section is provided with a feed rate faster than that of each belt conveyor in the primary steaming section and the secondary steaming section. A continuous rice cooking device including rotating first and second loosening machines.
JP62147311A 1987-06-13 1987-06-13 Continuous rice boiling device Granted JPS6328360A (en)

Priority Applications (1)

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

Applications Claiming Priority (1)

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

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP60041457A Division JPS61199820A (en) 1985-03-01 1985-03-01 Continuous rice cooking apparatus

Related Child Applications (5)

Application Number Title Priority Date Filing Date
JP5214591A Division JPH07108260B2 (en) 1993-08-01 1993-08-30 Continuous rice cooker
JP5214590A Division JP2510829B2 (en) 1993-08-30 1993-08-30 Continuous rice cooker
JP5214589A Division JPH07108259B2 (en) 1993-08-01 1993-08-30 Continuous rice cooker
JP5214592A Division JPH07108261B2 (en) 1993-08-01 1993-08-30 Continuous rice cooker
JP5214593A Division JP2510830B2 (en) 1993-08-30 1993-08-30 Continuous rice cooker

Publications (2)

Publication Number Publication Date
JPS6328360A JPS6328360A (en) 1988-02-06
JPH0469982B2 true JPH0469982B2 (en) 1992-11-09

Family

ID=15427324

Family Applications (1)

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

Country Status (1)

Country Link
JP (1) JPS6328360A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0223147U (en) * 1988-07-25 1990-02-15

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49101089U (en) * 1972-12-25 1974-08-30
JPS5532317U (en) * 1978-08-17 1980-03-01
JPS57169405U (en) * 1981-04-17 1982-10-25
JPS59224661A (en) * 1983-06-01 1984-12-17 Shinagawa Kogyosho:Kk Method and apparatus for cooking grains
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
JPS6328360A (en) 1988-02-06

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