JPS5823762A - Continuous steaming of sweet potato - Google Patents

Continuous steaming of sweet potato

Info

Publication number
JPS5823762A
JPS5823762A JP56121887A JP12188781A JPS5823762A JP S5823762 A JPS5823762 A JP S5823762A JP 56121887 A JP56121887 A JP 56121887A JP 12188781 A JP12188781 A JP 12188781A JP S5823762 A JPS5823762 A JP S5823762A
Authority
JP
Japan
Prior art keywords
conveyor
drainage
potatoes
potato
steamed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP56121887A
Other languages
Japanese (ja)
Inventor
Kenji Kanemitsu
兼光 賢二
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.)
HONBOU SYUZO KK
Original Assignee
HONBOU SYUZO 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 HONBOU SYUZO KK filed Critical HONBOU SYUZO KK
Priority to JP56121887A priority Critical patent/JPS5823762A/en
Publication of JPS5823762A publication Critical patent/JPS5823762A/en
Pending legal-status Critical Current

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  • Preparation Of Fruits And Vegetables (AREA)

Abstract

PURPOSE:To make a volume of device per production small and to obtain high- quality steamed sweet potatoes continuously, by setting a drainage conduit at a zone from the sweet potato feed part of the highest conveyor to the bottom of the conveyor, separating the initial drainage from the following drainage, followed by recovery. CONSTITUTION:The steaming chamber 10 is equipped with three step conveyors, the highest conveyor 11, the middle conveyor 12, the lowest conveyor 13. Sweet potatoes are fed from the rotary valve 14 for feeding raw material set at the top of the steaming chamber 10, steamed by the steam sent from the steam inlets 15, 16, and 17 while being transported on the conveyors along the arrow, and taken out from the outlet rotary valve 18. The drainage conduit 19 is set below the highest conveyor 11, and the initial drainage collected by this is discharged through the drainage pipe 20. The drainage produced in other positions is discharged through the drainage pipe 21 at the bottom of the steaming chamber 10 and used as water for preparation.

Description

【発明の詳細な説明】 本発明は芋焼酎を製造する際の2次仕込みの原料である
芋類を蒸す方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for steaming potatoes, which are the raw materials for the secondary preparation when producing potato shochu.

従来、芋焼酎製造における芋頭の蒸煮はバッチ弐芋蒸機
によって行なわれていた。つまり、種型の芋蒸機の中和
一定量の芋類を投入し、これを水蒸気により蒸煮し、空
気により強制的に冷却し、取出すという一連の方法であ
る。この方法はパンチ式操作に固有の非能率性に加え、
糧々の問題点を有していた。パッチ式操作では1回の操
作でなるべく多くの原料を地理することが望ましいが、
芋類の蒸煮においては量を多く仕込む程、蒸された下部
の芋が上部の芋の重量で押し潰される割合も多くカリ、
空気によって強制的に冷却する際、通風が悪くなり冷却
に長時間要するとともに送風機の能力もそれだけ大きな
もの和しなければならないという問題があって、1回の
仕込み量を制限せざるを得ない。その為生産量を上ける
ためkは多数の芋蒸機を必要とし、広い設置面積を要し
たa 1また、蒸煮の前後Kかいて芋の体積が変化する
とと、強制冷却のために芋蒸機の上下にかなりの空間を
設ける必要があること等の理由から生産量当たりの装置
容量が、相当大きなものになるという欠点も有していた
。更に、芋は選別によりまた工程中にかなり傷がつき、
蒸煮中に内部から糖質及び7澱粉質等、の有効成分がド
レン中に流出するが、バッチ式操作では芋の表面に附着
していた土、芋のヤニ、線虫等もこれと一緒にドレンと
して排出されるため有効成分の利用が図れず、かといっ
てそのまま廃棄すればBODが高いので公害防止のため
の処理を要した0ま走上記混入物は下層の芋に附着して
蒸芋の性状に悪影響を及ぼしていた。
Conventionally, steaming of sweet potato heads in the production of sweet potato shochu has been carried out using a batch two potato steamer. In other words, it is a series of methods in which a certain amount of neutralized potatoes is put into a seed-shaped potato steamer, steamed with steam, forcedly cooled with air, and taken out. In addition to the inefficiencies inherent in punch-style operations, this method
They had problems with food supply. In patch operation, it is desirable to cover as much raw material as possible in one operation;
When steaming potatoes, the larger the amount, the more the lower part of the steamed potato will be crushed by the weight of the upper part of the potato, and the higher the amount of potassium.
When forcibly cooling with air, there is a problem that ventilation is poor and cooling takes a long time, and the capacity of the blower must be increased accordingly, so the amount of preparation at one time has to be limited. Therefore, in order to increase production, a large number of potato steamers were required, which required a large installation area.1 Also, when the volume of potatoes changes before and after steaming, the forced cooling requires a large number of potato steamers. It also has the disadvantage that the equipment capacity per production volume is quite large because of the need to provide a considerable amount of space above and below. Furthermore, the potatoes are considerably damaged due to sorting and during the process.
During steaming, active ingredients such as carbohydrates and 7 starches flow out into the drain, but in batch-type operations, soil, tar, tar, nematodes, etc. that adhere to the surface of the potatoes are also washed away. Since it is discharged as drain, the active ingredients cannot be used, and if it is disposed of as is, the BOD is high, so treatment to prevent pollution is required.The above contaminants attach to the lower layer of potatoes and become steamed had a negative effect on the properties of

更Kまた、従来のパッチ式では蒸煮が完了すると人が芋
蒸機の中に入ってスコップ等で蒸芋の取出しを行゛なっ
ていたが、この作業は食品製造としては好ましいもので
はなく、また、蒸された芋の上で作業をするので足場が
悪く労災を惹き起こす危険もあった。
In addition, in the conventional patch method, once steaming was completed, a person had to go into the steamer and remove the steamed potatoes with a shovel, but this work was not desirable for food production, and Because workers worked on top of steamed potatoes, the footing was poor and there was a risk of work-related accidents.

本発明は上記欠点を解消すべくなされたものであって、
生産量当たりの装置容量が小さく、また有効成分を含有
するドレンを有効に利用することができるとともに品質
のよい蒸芋を製造することのできる芋蒸方法を提供する
ことを目的としてbる。
The present invention has been made to solve the above-mentioned drawbacks, and includes:
It is an object of the present invention to provide a method for steaming sweet potatoes that requires a small equipment capacity per production volume, can effectively utilize drains containing active ingredients, and can produce steamed potatoes of good quality.

本発明は、連続的に早撃を蒸煮する方法であり、蒸気室
内に多段に配置されたコンベヤの最上段のコンベヤに早
撃を連続的に供給し、早撃を順次下段のコンベヤに移送
しながら蒸煮するとともに、最上段コンベヤの早撃供給
部から一定移送距離に亘るコンベヤの下部にドレン溝を
配設して初期ドレンを以後のドレンと分けて回収するこ
とを特徴としている。
The present invention is a method of continuously steaming rapid fire, in which rapid fire is continuously supplied to the top conveyor of a conveyor arranged in multiple stages in a steam chamber, and the rapid fire is sequentially transferred to the lower conveyor. It is characterized in that a drain groove is disposed at the bottom of the conveyor over a fixed transfer distance from the quick-hit supply section of the top conveyor, and the initial drain is collected separately from the subsequent drain.

早撃社密閉状の蒸気室内に多段に重ねて配設されたコン
ベヤの最上段のコンベヤに供給され、コンベヤ上を順次
下段のコンベヤへと移送されながら蒸気により蒸煮され
る。コンベヤは移送する早撃が効果的に蒸煮されるよう
に蒸気がコンベヤの搬送面を通過できる構造となってい
る。このよう&構造の:yンペヤには例えば金網チェー
ンコンベヤ、多孔ベルトコンベヤ等があるが、蒸煮した
早撃忙よって目詰まりし難い構造のものを選択する必要
がある。例えば、互いにわずかな間隔をあけて平行に連
結されたローラーにより搬送面を形成すbようなコンベ
ヤが好ましい。最上段コンベヤの一つ下のコンベヤは最
上段コンベヤとけ反対方向に早撃を移送し、その下のコ
ンベヤはまた逆の方向、即ち、最上段コンベヤと同方向
に早撃を移送するというように早撃は左右に方向を変え
ながら下降し蒸気室から排出される。蒸気室は蒸気の効
率をよくするために密閉されており、早撃の入口及び出
口は蒸気を洩らさずに早撃を供給、取出できる機構を備
えている0蒸気室内を加圧状態にすれは蒸煮時間が短縮
されるのでコンベヤによる移送距離を短かぐすることが
でき、装置全体を小さくすることができる。一定温度一
定蒸気圧力下における早撃を蒸煮するだめの時間は略一
定であるので、コンベヤの移送速度を速くすればそれだ
け移送距離4長くなるので蒸気室の容積が大きくなり、
逆にコンベヤの移送速度を遅くすれば蒸気室の容積は小
さくなるが、同じ処理量で比較した場合はコンベヤの移
送速度が遅い程、コンベヤ上の芋の堆積量を増やさねば
ならず、それだけ芋の層高を高くする必要がある。然し
乍ら、あまり高過ぎると下部の芋が上部の芋の重量で押
し潰され、蒸気の通りが悪くなり、却って効率が悪くな
る。
It is supplied to the top conveyor of a multi-stage conveyor arranged in a sealed steam chamber, and is steamed by steam as it is sequentially transferred on the conveyor to the lower conveyor. The conveyor is constructed to allow steam to pass through the conveying surface of the conveyor so that the transported rapids are effectively steamed. There are several types of conveyors with this type of structure, such as wire mesh chain conveyors and perforated belt conveyors, but it is necessary to select one with a structure that does not easily clog due to the rapid speed of steaming. For example, it is preferable to use a conveyor such as b, in which the conveying surface is formed by rollers connected in parallel with each other at a small distance. The conveyor one level below the top conveyor transfers the quick hit in the opposite direction to the top conveyor, the conveyor below it also transfers the quick hit in the opposite direction, i.e. in the same direction as the top conveyor, and so on. The rapid fire descends while changing direction from side to side and is ejected from the steam chamber. The steam chamber is sealed to improve steam efficiency, and the quick-fire inlet and outlet are equipped with a mechanism that can supply and take out quick-fire without leaking steam.The steam chamber is pressurized. Since the steaming time is shortened, the conveyor distance can be shortened, and the entire apparatus can be made smaller. The time it takes to steam the rapid fire under constant temperature and constant steam pressure is approximately constant, so if the conveyor speed is increased, the conveyance distance 4 becomes longer, and the volume of the steam chamber increases.
Conversely, if the conveyor's transfer speed is slowed down, the volume of the steam chamber will be reduced, but when comparing the same throughput, the slower the conveyor's transfer speed, the more the amount of potatoes accumulated on the conveyor must be increased. It is necessary to increase the height of the layer. However, if the height is too high, the weight of the potatoes at the bottom will crush the potatoes at the top, making it difficult for steam to pass through, which will actually reduce efficiency.

本発明者はコンベヤ上の芋の高さを35e11以下にす
ることで芋が潰れることなくよく蒸気が通り効率よ〈蒸
煮できることを見い出した。
The present inventor has discovered that by setting the height of the potatoes on the conveyor to 35e11 or less, the potatoes can be steamed efficiently without being crushed and steam can pass through.

蒸気室に投入された早撃は温度が低いので蒸気がこれに
接触すると液化してドレンとなる。投入される早撃は洗
浄されていると祉いえ、土、ヤニ等が若干残っており、
これらは先ず投入後液化した蒸気忙よって洗い流される
。この段階では早撃は未だ蒸煮されていなりので芋の有
効成分は流れ出ない。この初期段階で生じたドレンはコ
ンベヤの下に配設されたドレン溝に滴り落ち、排出され
る。初期ドレン回収時間あるいは初期ドレン溝長さは投
入する早撃の汚れ具合、有効成分の流出の程度等を勘案
して決定される。以後に生ずるドレンは蒸気室底部のド
レン排出口から−まとめにして排出される。このドレン
KFi土、ヤニ等の汚物が混入していないので仕込み水
として利用でき、これに含有されている糖質及び澱粉質
等の有効成分の回収が図れる。
The temperature of the rapid fire put into the steam chamber is low, so when the steam comes into contact with it, it liquefies and becomes drain. It can be said that the quick shot that is put in has been cleaned, but there is some dirt, tar, etc. left.
These are first washed away by the liquefied steam after being added. At this stage, the sweet potato has not yet been steamed, so the active ingredients in the sweet potato have not leaked out. The condensate generated at this initial stage drips into a drain groove located below the conveyor and is discharged. The initial drain collection time or the initial drain groove length is determined by taking into account the degree of contamination of the input rapid shot, the degree of outflow of the active ingredient, etc. Subsequently generated condensate is collectively discharged from the condensate outlet at the bottom of the steam chamber. Since this drain KFi is not contaminated with dirt such as soil and tar, it can be used as water for preparation, and active ingredients such as carbohydrates and starch contained therein can be recovered.

以下、添附図面に示した望ましい実施例に基づいて本発
明を更に説明する。
The present invention will be further described below based on preferred embodiments shown in the accompanying drawings.

添附図面は本発明の連続芋蒸方法に使用される装置の一
実施例の簡略化した正面図である。
The accompanying drawing is a simplified front view of one embodiment of the apparatus used in the continuous potato steaming method of the present invention.

蒸気室lO内には上段、中段、下段の3機のコンベヤ1
1 、12 、13が配設されている。早撃は蒸気室1
0の上部に配設された原料投入ロータリーパルプ14か
ら投入され、矢標に沿ってコンベヤ上を移送されながら
、蒸気供給口15 、16 、17から供給された水蒸
気によって蒸煮され、出ロロータリーパルブ18から取
出される。上じコンベヤ11の下部にはドレン溝19が
配設されており、これによって集められた初期ドレンは
排水口2DKよって排出されるーその他の場所で生じた
ドレンは蒸気室lOの底部の排水口4かも排出され、仕
込み水として利用される。
There are three conveyors in the steam room IO: upper, middle, and lower.
1, 12, and 13 are arranged. Quick attack is steam room 1
The raw material is inputted from the input rotary pulp 14 arranged at the upper part of the rotary pulp, and while being transferred on the conveyor along the arrow mark, it is steamed by the steam supplied from the steam supply ports 15, 16, and 17, and then the rotary pulp 18. A drain groove 19 is provided at the bottom of the upper conveyor 11, and the initial drain collected thereby is discharged through the drain port 2DK - drain generated in other locations is drained through the drain port 4 at the bottom of the steam chamber IO. The water is discharged and used as water for preparation.

次に上記装置を用いて本発明を実施し次結果を示す。Next, the present invention was carried out using the above apparatus, and the following results are shown.

〔実施例〕〔Example〕

上記の装置によ〈洗浄、選別された甘藷を連続的に投入
して蒸煮を実施した。コンベヤ上の甘藷の高さを35c
m以上にすると下部の甘藷が押し潰される傾向が増大し
、蒸煮が効率的に行なわれなかった◇甘藷の高さを35
e11以下にした場合は約父分程度で完全に蒸煮するこ
とができ、得られた蒸せ藷の形状も原形を維持していた
。上段コンベヤで生ずるドレンが分離され、これらのド
レンが下段の充分蒸煮された甘藷に滴り落ちるととがな
いので、得られた蒸せ藷は香り、味、色が新鮮であった
。この蒸せ藷で仕込んだもろみは表面に浮上物も認めら
れず、出来た焼酎は香味が淡餐でしかも美味であった。
The washed and sorted sweet potatoes were continuously fed into the above-mentioned apparatus and steamed. The height of sweet potatoes on the conveyor is 35c.
If the height is more than 35 m, the sweet potato at the bottom tends to be crushed and steaming cannot be done efficiently.
When the temperature was lower than e11, the steamed potatoes could be completely steamed in about an hour's worth, and the shape of the resulting steamed potatoes maintained their original shape. The drain produced on the upper conveyor is separated and drips onto the fully steamed sweet potatoes in the lower layer, so that the resulting steamed sweet potatoes have a fresh aroma, taste, and color. No floating substances were observed on the surface of the moromi prepared with this steamed rice, and the resulting shochu had a light flavor and was delicious.

なお、本方法は連続式で行なうため、従来のバッチ式に
比較して単位生産量当たりに要する水蒸気の量が大幅に
減少した。
Furthermore, since this method is carried out in a continuous manner, the amount of steam required per unit of production is significantly reduced compared to the conventional batch method.

以上説明しえように本発明によれば品質のよい蒸芋を小
さい装置容積で経済的に効率よく生産できるとともk、
従来のパンチ式装置のように人力に頼る工程を省くこと
ができるので衛生上、安全上の問題も解決することがで
き、当業界に’4益するところ多大である0
As explained above, according to the present invention, high-quality steamed potatoes can be produced economically and efficiently with a small equipment volume.
Since it eliminates the process of relying on human power like the conventional punch-type device, it also solves hygiene and safety issues, which has great benefits for the industry.

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

添附図面は本発明の連続芋蒸方法に使用される装置の一
実施例の簡略化した正面図である。 10・・・蒸気室 11・・・上段コンベヤ 12・・
・中段プンヘ−?13・・・下段コンベヤ 14・・・
fl料投入a−pat−パルプ 15 、16 、17
・・・蒸気供給口 18・・・出口。 −タリーパルプ 19・・・ドレン溝 I、21・・・
排水口特許出願人  本坊酒造株式会社
The accompanying drawing is a simplified front view of one embodiment of the apparatus used in the continuous potato steaming method of the present invention. 10... Steam room 11... Upper conveyor 12...
・Middle Punghae? 13...lower conveyor 14...
fl feed input a-pat-pulp 15, 16, 17
...Steam supply port 18...Exit. -Tally pulp 19...Drain groove I, 21...
Drain port patent applicant Honbo Sake Brewery Co., Ltd.

Claims (1)

【特許請求の範囲】 ill蒸気室内に多段に配置されたコンベヤの最上段の
コンベヤに芋類を連続的に供給し、芋類を順次下段のコ
ンベヤに移送しながら蒸煮するとともに、最上段コンベ
ヤの芋類供給部から一定移送距111KMるコンベヤの
下部にドレン溝を配設して初期ドレyを以螢のドレンと
分けて回収することを特徴とする連続芋蒸方法。 (2)多段コンベヤを上中下3段として配設し、上段コ
ンベヤの下部に初期ドレンを回収するためのドレン溝を
配設して特許請求の範囲第(1)項に記載の連続芋蒸方
法。 (3)  コンベヤで移送される芋類の層高を35(至
)以下とした特許請求の範S第111項または第(2)
項に記載の連続芋蒸方法。 (41芋類が甘藷である特許請求の範a第(11項乃至
第(3)項に記載の連続芋蒸方法0
[Claims] Potatoes are continuously supplied to the top conveyor of the conveyors arranged in multiple stages in the ill steam chamber, and the potatoes are steamed while being sequentially transferred to the lower conveyor. A continuous potato steaming method characterized in that a drain groove is provided at the bottom of a conveyor that travels a fixed distance of 111 km from a potato supply section to separate and collect initial drain from subsequent drain. (2) Continuous potato steaming according to claim (1), in which a multi-stage conveyor is arranged as three stages, upper, middle and lower, and a drain groove for collecting initial drain is arranged at the lower part of the upper stage conveyor. Method. (3) Claim S Clause 111 or (2) in which the layer height of potatoes transported by a conveyor is 35 (to) or less
Continuous potato steaming method described in section. (41) Continuous potato steaming method according to claim a (claim 11 to (3)) in which the potato is sweet potato
JP56121887A 1981-08-05 1981-08-05 Continuous steaming of sweet potato Pending JPS5823762A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56121887A JPS5823762A (en) 1981-08-05 1981-08-05 Continuous steaming of sweet potato

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56121887A JPS5823762A (en) 1981-08-05 1981-08-05 Continuous steaming of sweet potato

Publications (1)

Publication Number Publication Date
JPS5823762A true JPS5823762A (en) 1983-02-12

Family

ID=14822364

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56121887A Pending JPS5823762A (en) 1981-08-05 1981-08-05 Continuous steaming of sweet potato

Country Status (1)

Country Link
JP (1) JPS5823762A (en)

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