JPS6211584B2 - - Google Patents

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Publication number
JPS6211584B2
JPS6211584B2 JP4453384A JP4453384A JPS6211584B2 JP S6211584 B2 JPS6211584 B2 JP S6211584B2 JP 4453384 A JP4453384 A JP 4453384A JP 4453384 A JP4453384 A JP 4453384A JP S6211584 B2 JPS6211584 B2 JP S6211584B2
Authority
JP
Japan
Prior art keywords
steam injection
steamed rice
injection means
passage
rice
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
Application number
JP4453384A
Other languages
Japanese (ja)
Other versions
JPS60188054A (en
Inventor
Shiro Hagiwara
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.)
GUNMA NETSU KANRI SENTAA KK
Original Assignee
GUNMA NETSU KANRI SENTAA 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 GUNMA NETSU KANRI SENTAA KK filed Critical GUNMA NETSU KANRI SENTAA KK
Priority to JP59044533A priority Critical patent/JPS60188054A/en
Publication of JPS60188054A publication Critical patent/JPS60188054A/en
Publication of JPS6211584B2 publication Critical patent/JPS6211584B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は清酒製造工程中等における蒸米の製造
方法及びその装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for producing steamed rice in a sake production process and the like.

従来この蒸米製造装置としては、第1図に示す
ような蒸米Aを収納したセイロBに対して下部よ
り例えば、水収納タンクC内に位置する蒸気発生
用ヒーテイングコイルDこの上方に位置する加熱
ヒーテイングコイルD′により加熱蒸気を与え蒸
し作用を施すセイロ蒸し方法、或いは第2図に示
すように上面に蓋またはシートを被着させた木樽
Eを用い、木樽E内の、すのこF上の蒸米Aに対
して、すのこF下面の蒸気噴出部Gより蒸気噴射
し、所要の蒸し作用を施す方法、或いは第3図に
示す如く上下開放型の筒H内に蒸米Aを上方より
入れ、下方部分にて蒸気噴射口Iにより蒸気噴射
を受け下方開口部より排出されコンベアJより移
送されてゆく立型蒸米機。
Conventionally, in this steamed rice manufacturing apparatus, a steamer B containing steamed rice A as shown in FIG. Using a steamer steamer method in which heated steam is applied by a heating coil D' to perform a steaming action, or by using a wooden barrel E with a lid or sheet on the top surface as shown in Fig. Steam is injected from the steam jetting part G on the lower surface of the drainboard F to the steamed rice A above to give the desired steaming effect, or the steamed rice A is put into a vertically open cylinder H from above as shown in Fig. 3. , a vertical rice steaming machine in which steam is ejected from the steam injection port I at the lower part, and the rice is discharged from the lower opening and transferred from the conveyor J.

さらにはコンベアにより連続して移送され通路
通過中に蒸気噴射により蒸し作用を施す連続蒸し
機が存在するが、前述したセイロ形式の蒸し装置
にあつては、蒸米が含有している脂肪酸が自然に
発散放出されていたが、清酒の蒸米製造のように
大量の蒸米を必要とするものには不向きであり、
かつ生産効率、作業効率とも劣るという欠点を有
する。また前述した形態の連続蒸し機、或いは立
型蒸米機にあつては、生産効率、作業効率はセイ
ロ蒸しに比較して良くとも、脂肪酸が抜けること
なく蒸されるため仕上がりの香が悪いという欠
点、酸化して腐敗しやすく色変化あるいは出来上
がり後酢味が出やすくなるという欠点があり品質
的にも悪い結果を生んでいるのが現状である。
Furthermore, there are continuous steamers that are continuously transported by a conveyor and steamed by steam injection while passing through a passage, but in the case of the above-mentioned steamer steamer, the fatty acids contained in the steamed rice are naturally absorbed. However, it is not suitable for processes that require a large amount of steamed rice, such as the production of steamed rice for sake.
Moreover, it has the disadvantage of being inferior in both production efficiency and work efficiency. In addition, although the production efficiency and work efficiency of the above-mentioned continuous steamer or vertical rice steamer are better than that of steamer steamer, the disadvantage is that the finished product has a bad aroma because the fatty acids are steamed without being removed. However, the current situation is that it is easily oxidized and putrefied, and that it tends to change color or give off a vinegar taste after completion, resulting in poor quality results.

すなわち立型蒸米機の場合には、蒸米中で発生
した脂肪酸は下部より上部へ蒸気が上がる時に持
つて行くために蒸し上がりの香が良くないという
欠点、また従来の連続蒸米機にあつても蒸気を逃
さないために脂肪酸が蓄積されたまま蒸し上がる
ため、前述した如き欠点を解消できない。
In other words, in the case of a vertical rice steamer, fatty acids generated during steaming are carried away when the steam rises from the bottom to the top, so the aroma after steaming is not good.Also, in the case of a conventional continuous rice steamer, In order to prevent steam from escaping, the fatty acids are steamed while being accumulated, so the above-mentioned drawbacks cannot be overcome.

また、蒸米については昔から経験的にまた原則
論的に言われている通り、蒸米製造の初期には
程々の加温でまた中期には強熱で米の中芯を炊き
上げ、後期には米の表面の余分な水分を取り去り
中心が軟かくふつくらとし外面はべとつかずやや
硬い表面を作ることが理想的とするものである。
この「内軟外硬」の蒸米は清酒製造に要する蒸米
としても全く理想的なものとして要求されてい
る。即ち、酒米に於いては中心と外表面が同じ硬
さであると清酒製造工程に於いて全体的に溶解し
軟らかい糊状になり濁りが生じ、「内軟外硬」の
蒸米であれば米の中心部のみが酒源となり最終的
には中空となり外表面のみが残余物となり、生産
効率の良い高品質の清酒製造を目的とするには理
想的なものである。生産効率、作業効率等の点で
最も比較せねばならぬ従来の連続蒸し機に於いて
はこの点に於いて検討が加えられていないもので
ある。
Regarding steamed rice, it has long been said both empirically and in principle that in the early stages of steamed rice production, the center of the rice is cooked with moderate heating, and in the middle stage, the center of the rice is cooked, and in the later stage, the core of the rice is cooked. The ideal method is to remove excess moisture from the surface of the rice, leaving the center soft and plump, while the outside is not sticky and has a slightly hard surface.
This steamed rice with a soft inside and a hard outside is required as the ideal steamed rice for sake production. In other words, if the center and outer surface of sake rice are the same hardness, the entire surface will dissolve during the sake manufacturing process, becoming a soft paste and becoming turbid. Only the center of the rice becomes the source of sake, and in the end it becomes hollow and only the outer surface remains, making it ideal for producing high-quality sake with good production efficiency. This point has not been studied in the conventional continuous steamer, which should be compared most in terms of production efficiency and working efficiency.

本発明は生産効率、作業効率良く連続して蒸米
を製造することができるとともに、蒸米中に脂肪
酸を強制的に放出する機能的な手段を備え且つ蒸
米製造上の初期、中期、後期段階に於いてそれぞ
れ適切な蒸気或いは加熱手段による熱供給を行
い、香も良く高品質の蒸米を製造することのでき
る蒸米の製造方法及びその装置を提供することを
目的とする。
The present invention is capable of continuously producing steamed rice with high production efficiency and work efficiency, and is equipped with a functional means for forcibly releasing fatty acids during steaming, and can be used in the early, middle, and late stages of steamed rice production. An object of the present invention is to provide a method and apparatus for producing steamed rice that can produce high-quality steamed rice with a good aroma by supplying heat with appropriate steam or heating means.

第4図中1はカバーであり、該カバーは下方が
開放されていてもよく、該カバーにより形成され
る通路2内にはネツトコンベア3が配置され、他
のコンベア4により移送されてきた蒸米5を移送
するものである。
Reference numeral 1 in FIG. 4 is a cover, and the cover may be open at the bottom. A net conveyor 3 is arranged in the passage 2 formed by the cover, and the steamed rice transferred by another conveyor 4 is placed in the passage 2 formed by the cover. 5.

図中6はネツトコンベア3下面の上面開口ボツ
クス7,8内に取付けられネツトコンベア3下面
よりネツトコンベア3上の蒸米5に対し生蒸気噴
射をする生蒸気噴射手段である。この段階でまず
蒸米に水分を与え例えば100℃以下の蒸し作用を
施しつつ、移送してゆく。9は生蒸気噴射手段6
の次段に位置し、通路上方よりネツトコンベア3
上の蒸米に対し上方より加熱蒸気噴射作用を施す
加熱蒸気噴射手段であり、下面開口ボツクス10
内の蒸気噴射装置11と加熱ヒーター12の組合
わせからなり、当該個所において、例えば100℃
前後の蒸気を加熱ヒーターによつて103℃〜105℃
まで加熱し、前段より高温の雰囲気中にて加熱蒸
気噴射を蒸米に対して施すものであり、前段にお
いて発生した脂肪酸或いはこの段階で発生した脂
肪酸も、この段階にて蒸米中より排出され蒸気噴
射装置11及び加熱ヒーター12の設定個所に対
応する位置でネツトコンベア3下面に形成された
排気手段13により通路2外部に放出されてゆく
ものである。14は脱脂肪酸工程を経た蒸米に対
して仕上げのための蒸しを施すネツトコンベア3
下面に位置する上面開口のボツクス15内に位置
する加熱蒸気噴射手段であり、蒸気噴射装置1
6、加熱ヒーター17の組合わせからなり蒸米に
対して新たに清浄な蒸気を噴射するとともに加熱
ヒーター17により蒸米表面の水分を除去し、外
表面が硬く内表面は軟らかくふつくらとした蒸米
を得るものである。
In the figure, reference numeral 6 denotes a live steam injection means that is installed in the upper opening boxes 7 and 8 on the bottom surface of the net conveyor 3 and injects live steam into the steamed rice 5 on the net conveyor 3 from the bottom surface of the net conveyor 3. At this stage, the steamed rice is first moisturized and then steamed at a temperature of, for example, 100°C or less, while being transported. 9 is live steam injection means 6
Net conveyor 3 is located on the next stage from above the aisle.
It is a heated steam injection means that applies a heated steam injection action to the steamed rice on the top from above, and has a bottom opening box 10.
It consists of a combination of a steam injection device 11 and a heating heater 12, and the temperature at that location is, for example, 100°C.
Heater heats the steam before and after to 103℃~105℃
The steamed rice is then heated to a temperature higher than that of the previous stage, and the steamed rice is injected with heated steam in an atmosphere higher than that of the previous stage.The fatty acids generated in the previous stage or the fatty acids generated at this stage are also discharged from the steamed rice at this stage and are injected with steam. The liquid is discharged to the outside of the passage 2 by an exhaust means 13 formed on the lower surface of the net conveyor 3 at a position corresponding to the setting position of the device 11 and the heating heater 12. 14 is a net conveyor 3 that performs finishing steaming on the steamed rice that has undergone the fatty acid removal process.
It is a heated steam injection means located in a box 15 with an upper opening located on the lower surface, and is a steam injection device 1.
6. Consisting of a combination of heating heaters 17, new clean steam is injected onto the steamed rice, and the heating heater 17 removes moisture from the surface of the steamed rice to obtain steamed rice with a hard outer surface and a soft inner surface. It is something.

尚、本実施例の場合には、蒸気噴射装置11、
加熱ヒーター12はネツトコンベア3上面に取り
付けたがこれは前段において蒸気をネツトコンベ
ア3下面より上面に向けて噴射することから、蒸
気中の脂肪酸がネツトコンベア3上に存在するこ
とから必然的にその効率上、その位置を特定した
が、ネツトコンベア3下方に取付け、加熱蒸気噴
射をし、蒸気とともに脂肪酸をネツトコンベア上
方に設けた排気手段により排出することも可能で
あるし、また生蒸気噴射手段6をネツトコンベア
3上面に設け、加熱蒸気噴射手段9をネツトコン
ベア3下面に設け、これに伴い仕上げのための加
熱蒸気噴射手段をネツトコンベア3上面に取付け
形成することも勿論可能である。
In addition, in the case of this embodiment, the steam injection device 11,
The heating heater 12 was attached to the top surface of the net conveyor 3, but this is because the steam is injected from the bottom surface of the net conveyor 3 toward the top surface in the previous stage, and fatty acids in the steam are present on the net conveyor 3. For efficiency reasons, the location has been specified, but it is also possible to install it below the net conveyor 3, inject heated steam, and discharge the fatty acid together with the steam by an exhaust means installed above the net conveyor. Of course, it is also possible to provide the heated steam injection means 9 on the upper surface of the net conveyor 3 and the heated steam injection means 9 on the lower surface of the net conveyor 3, and to attach and form the heated steam injection means for finishing on the upper surface of the net conveyor 3.

しかして本発明によれば、蒸米には必要最少限
の熱を使用するが、蒸米吸収熱カロリーの約30〜
50%を多量に送蒸して、その余剰の蒸気を脂肪酸
のために使うという基本的な発想を下に、通路途
中に機能的な脱脂肪酸手段を設け、脂肪酸をスム
ーズに効率良く強制放出することができたことか
ら、さらには蒸米製造上の初期、中期、後期段階
に於いてそれぞれ適切な蒸気或いは加熱手段によ
る熱供給を行なつたから、連続蒸米製造にあつて
も、香良く色変化或いは製品が酢味化することを
防ぐことのできる高品質の蒸米を生産効率、作業
効率良く製造することができ、従来の蒸米製造装
置の諸欠点を全て解決できたものである。
However, according to the present invention, the minimum amount of heat necessary for steaming rice is used, but approximately 30 to 30
Based on the basic idea of steaming a large amount of 50% and using the excess steam for fatty acids, we installed a functional fatty acid removal means in the middle of the passage to forcefully release fatty acids smoothly and efficiently. Furthermore, since heat is supplied by appropriate steam or heating means at the early, middle, and late stages of steamed rice production, even in continuous steamed rice production, the product can be flavored, color-changed, or finished. It is possible to produce high-quality steamed rice that can prevent rice from becoming vinegary with high production efficiency and work efficiency, and it has solved all the drawbacks of conventional steamed rice production equipment.

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

第1図より第3図は従来の蒸米製造装置を示す
断面図、第4図は本発明の蒸米製造装置を示す断
面説明図である。 1……カバー、2……通路、3……ネツトコン
ベア、5……蒸米、6……生蒸気噴射手段、9,
14……加熱蒸気噴射手段、12,17……加熱
ヒーター。
1 to 3 are cross-sectional views showing a conventional steamed rice manufacturing apparatus, and FIG. 4 is a cross-sectional explanatory view showing the steamed rice manufacturing apparatus of the present invention. 1... Cover, 2... Passage, 3... Net conveyor, 5... Steamed rice, 6... Live steam injection means, 9.
14... Heating steam injection means, 12, 17... Heating heater.

Claims (1)

【特許請求の範囲】 1 コンベアにより移送されてくる蒸米に対し
て、通路通過中に蒸気により所要の蒸し作用を施
す連続蒸米方法において、通路中に生蒸気噴射手
段により蒸米に水分を与え且つ蒸し作用を施し、
次に加熱蒸気噴射手段により前記生蒸気噴射手段
よりは高温にて蒸米に蒸し作用を施し且つ前記加
熱蒸気噴射手段に対応する排気手段により蒸気と
ともに排出される脂肪酸を通路外部に放出し、さ
らに後方には加熱蒸気噴射手段により蒸米に仕上
げの蒸し作用を施すことを特徴とする蒸米の製造
方法。 2 コンベア上の蒸米に対して通路前方部には蒸
米に水分を与え蒸し作用を施す生蒸気噴射手段、
通路中途部上方には蒸気噴射装置と加熱ヒーター
からなる加熱蒸気噴射手段、前記加熱蒸気噴射手
段に対応するコンベア下方には、蒸気とともに排
出される脂肪酸を通路外部に排出するための排気
手段、通路後方部には仕上げのための蒸気噴射装
置と加熱ヒーターからなる加熱蒸気噴射手段を設
けたことを特徴とする蒸米の製造装置。 3 特許請求の範囲第2項記載の加熱蒸気噴射手
段は、通路中途部のコンベア下方に設け、コンベ
ア上の蒸米に対し下面より加熱蒸気噴射を行うと
ともに、この加熱蒸気噴射手段に対応するコンベ
ア上方には蒸気とともに排出される脂肪酸を通路
外部に排出するための排気手段を設けたことを特
徴とする蒸米の製造装置。
[Claims] 1. In a continuous rice steaming method in which steamed rice transferred by a conveyor is subjected to a required steaming action with steam while passing through a passage, the steamed rice is moistened and steamed by a live steam injection means in the passage. perform the action,
Next, the heated steam injection means steams the steamed rice at a higher temperature than the live steam injection means, and the exhaust means corresponding to the heated steam injection means discharges the fatty acid discharged together with the steam to the outside of the passage, and further back. A method for producing steamed rice, which comprises applying a finishing steaming action to the steamed rice using heated steam injection means. 2 Live steam injection means for adding moisture to the steamed rice and applying a steaming action to the steamed rice on the conveyor at the front part of the passage;
A heated steam injection means consisting of a steam injection device and a heating heater is provided above the midway part of the passage, and an exhaust means for discharging fatty acids discharged together with the steam to the outside of the passage is provided below the conveyor corresponding to the heated steam injection means, and a passage. 1. A steamed rice manufacturing apparatus characterized in that a heating steam injection means consisting of a finishing steam injection device and a heating heater is provided in the rear part. 3. The heated steam injection means recited in claim 2 is provided below the conveyor in the middle of the passage, and injects heated steam to the steamed rice on the conveyor from the bottom surface, and at the same time, the heated steam injection means is provided above the conveyor corresponding to the heated steam injection means. An apparatus for producing steamed rice, characterized in that the apparatus is provided with an exhaust means for discharging fatty acids discharged together with steam to the outside of the passage.
JP59044533A 1984-03-08 1984-03-08 Preparation of steamed rice and its device Granted JPS60188054A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59044533A JPS60188054A (en) 1984-03-08 1984-03-08 Preparation of steamed rice and its device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59044533A JPS60188054A (en) 1984-03-08 1984-03-08 Preparation of steamed rice and its device

Publications (2)

Publication Number Publication Date
JPS60188054A JPS60188054A (en) 1985-09-25
JPS6211584B2 true JPS6211584B2 (en) 1987-03-13

Family

ID=12694142

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59044533A Granted JPS60188054A (en) 1984-03-08 1984-03-08 Preparation of steamed rice and its device

Country Status (1)

Country Link
JP (1) JPS60188054A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5282796A (en) * 1975-12-29 1977-07-11 Masahiko Izumi Suction boiling method of grains
JPS58859A (en) * 1981-06-22 1983-01-06 Nippon Shinyaku Co Ltd Improving composition of food and improving method

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5282796A (en) * 1975-12-29 1977-07-11 Masahiko Izumi Suction boiling method of grains
JPS58859A (en) * 1981-06-22 1983-01-06 Nippon Shinyaku Co Ltd Improving composition of food and improving method

Also Published As

Publication number Publication date
JPS60188054A (en) 1985-09-25

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