JP3056947B2 - Moromi mashing tank - Google Patents

Moromi mashing tank

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Publication number
JP3056947B2
JP3056947B2 JP12103594A JP12103594A JP3056947B2 JP 3056947 B2 JP3056947 B2 JP 3056947B2 JP 12103594 A JP12103594 A JP 12103594A JP 12103594 A JP12103594 A JP 12103594A JP 3056947 B2 JP3056947 B2 JP 3056947B2
Authority
JP
Japan
Prior art keywords
raw material
tank
stirring shaft
spiral
blades
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
JP12103594A
Other languages
Japanese (ja)
Other versions
JPH07322871A (en
Inventor
展裕 長谷川
隆司 寺垣
哲男 小林
忠明 宮田
Original Assignee
神鋼パンテツク株式会社
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 神鋼パンテツク株式会社 filed Critical 神鋼パンテツク株式会社
Priority to JP12103594A priority Critical patent/JP3056947B2/en
Publication of JPH07322871A publication Critical patent/JPH07322871A/en
Application granted granted Critical
Publication of JP3056947B2 publication Critical patent/JP3056947B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Mixers Of The Rotary Stirring Type (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】本発明はもろみの仕込槽に関し、
特に詳しくは清酒製造に適した装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a mashing tank.
More particularly, it relates to an apparatus suitable for sake production.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】本発
明の理解のために、最初に清酒の製造方法の概略につい
て説明する。清酒の製造においては、まず原料米を精白
し、次いで蒸して蒸米とし、この蒸米の一部で麹をつく
る。そして、蒸米の一部に麹、水および種酵母を添加し
て酒母が作られる。このとき、雑菌の繁殖を抑えるため
に、乳酸、酵母の栄養源となる「リン酸カリウム」など
のミネラル類が加えられることもある。このようにして
できた酒母に蒸米、麹および水を加えて仕込み、もろみ
のアルコール醗酵が行われる。この醗酵の終わったもろ
みは圧搾されて液部(清酒)と固形部(酒粕)に分離さ
れる。この場合、配合に応じて、もろみの圧搾工程の前
に醸造アルコールの添加や、醸造用糖類の添加(一般的
に「4段添加」と呼ばれている)が行われることがあ
る。そして、圧搾された清酒は通常加熱殺菌してタンク
に貯蔵し、出荷時に調合して瓶詰される。
2. Description of the Related Art In order to understand the present invention, an outline of a method for producing sake is first described. In the manufacture of sake, rice is first refined and then steamed to steamed rice, and a portion of the steamed rice is used to make koji. Then, koji, water and a seed yeast are added to a part of the steamed rice to make a sake mother. At this time, minerals such as lactic acid and “potassium phosphate” which is a nutrient source of yeast may be added in order to suppress the propagation of various bacteria. Steamed rice, koji and water are added to the sake brewer thus prepared, and the mash is subjected to alcoholic fermentation. The moromi after the fermentation is squeezed and separated into a liquid part (sake) and a solid part (sake lees). In this case, depending on the composition, addition of brewing alcohol or addition of brewing sugar (generally referred to as “four-stage addition”) may be performed before the moromi squeezing step. The squeezed sake is usually sterilized by heating and stored in a tank.

【0003】上記した清酒の製造においては、仕込原料
の櫂入れ(混合)や温度管理などに杜氏を始めとする熟
練した作業者の経験と勘に頼るところが多かったが、近
年、製造管理の省力化、合理化を図るため、清酒製造用
の仕込槽として、外套付き機械撹拌装置が開発され、実
用化されている。例えば、図4に示すように、モータ2
1に接続した撹拌軸22に切り込み撹拌翼23を取り付
けた撹拌装置が知られている(実開昭51−9094号
公報参照)。この撹拌装置によれば、固形分が多く蒸米
が膨潤して固化状態となる仕込初期においては、手作業
の荒櫂に近い操作は可能であるが、固形物の移動が悪
く、固形物の上下移動が促進されないので、品質・温度
管理(以下「品温管理」という)が十分に行えないとい
う欠点がある。さらに、蒸米が液化、糖化して固形物量
が少なくなって流動しやすい状態になると、この種の撹
拌装置による仕込みでは液状原料の流動撹拌が不十分
で、外套24を流通する流体との間の熱交換が良好に行
われず、品温管理が極めて不満足なものとなる。さら
に、上記した4段添加やアルコール添加時の撹拌混合も
十分に行えないという欠点がある。
[0003] In the production of the above-mentioned sake, many people rely on the experience and intuition of skilled workers, such as Toji, in padding (mixing) and temperature control of the raw materials, but in recent years, labor has been reduced in production control. In order to streamline and streamline, a mechanical stirring device with a jacket has been developed and put into practical use as a brewing tank for sake production. For example, as shown in FIG.
There is known a stirrer in which a stirrer 23 is attached to a stirrer shaft 22 connected to a stirrer 1 (see Japanese Utility Model Laid-Open No. 51-9094). According to this stirrer, in the initial stage of preparation in which steamed rice swells and solidifies due to a large amount of solid content, an operation close to a manual rough paddle is possible, but the movement of the solid material is poor, and the solid material is moved up and down. Since the movement is not promoted, there is a drawback that quality / temperature management (hereinafter referred to as “product temperature management”) cannot be performed sufficiently. Furthermore, when the steamed rice is liquefied and saccharified and the solid content is reduced to a state where it is easy to flow, flow stirring of the liquid raw material is insufficient in the preparation with this type of stirring device, and the flow between the fluid flowing through the mantle 24 is not sufficient. Heat exchange is not performed well, and product temperature management becomes extremely unsatisfactory. Further, there is a disadvantage that the above-described four-stage addition and stirring and mixing at the time of alcohol addition cannot be sufficiently performed.

【0004】また、2ないし3段のパドル翼またはター
ビン翼を備えた撹拌装置では、蒸米が液化、糖化してか
らの流動しやすい段階での撹拌混合は可能であるが、固
形物量の多い仕込初期には『荒櫂入れ』という切り返し
撹拌が行えず、蒸米粒を機械的に破砕して糊化してしま
う欠点がある。
[0004] In addition, in a stirring apparatus having two or three stages of paddle blades or turbine blades, stirring and mixing can be performed at a stage where steamed rice is easily liquefied and saccharified and then fluidized. In the early stage, it is not possible to perform the reciprocating agitation of “rough paddle”, and there is a disadvantage that steamed rice grains are mechanically crushed and gelatinized.

【0005】本発明は従来の技術の有するこのような問
題点に鑑みてなされたものであって、その目的は、食
品、特に清酒の製造において、仕込原料である蒸米の仕
込初期の固形物状態での切り返しおよび上下攪拌と液
化、糖化後の流動状態における攪拌混合を十分に行い、
良好な品質管理状態のもとで高品質の清酒を製造するこ
とが可能なもろみの仕込槽を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art, and has as its object to prepare a solid state of steamed rice, which is a raw material, in the initial stage of preparation in the production of foods, particularly sake. Turn over and up and down stirring and liquefaction, perform sufficient stirring and mixing in the fluidized state after saccharification,
It is an object of the present invention to provide a moromi mashing tank capable of producing high-quality sake under good quality control conditions.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に本発明の要旨は、胴部と底部に外套を有する筒状の原
料仕込槽の中心部鉛直方向に回転自在に主攪拌軸を配
し、上記原料仕込槽の内面に近接して螺旋状に形成され
た螺旋翼を配し、上記主攪拌軸から半径方向に延設した
複数の支持腕に該螺旋翼を接続し、主攪拌軸下端部にパ
ドル翼を固定し、さらに、主攪拌軸と螺旋翼との間にお
いて鉛直方向に原料仕込槽内の原料を切り崩すための切
羽根を設けたことを特徴とするもろみの仕込槽を第一の
発明とし、上記第一の発明において、切羽根の断面形状
が回転方向に先細り状であることを特徴とするもろみの
仕込槽を第二の発明とする。
SUMMARY OF THE INVENTION In order to achieve the above object, the gist of the present invention is to provide a main stirring shaft rotatable in the vertical direction at the center of a cylindrical raw material charging tank having a shell at a body and a bottom. A spiral blade formed in a spiral shape is arranged near the inner surface of the raw material charging tank, and the spiral blade is connected to a plurality of support arms extending in a radial direction from the main stirring shaft. A paddle blade is fixed to a lower end portion, and further, a cutting blade for cutting down a raw material in a raw material charging tank is provided between a main stirring shaft and a spiral blade in a vertical direction. According to a first aspect of the present invention, in the first aspect, a moromi mashing tank is characterized in that the sectional shape of the cutting blade is tapered in the rotation direction.

【0007】[0007]

【作用】原料仕込槽に、仕込水と麹米(必要に応じて液
化酵素、糖化酵素を添加したもの)と蒸米と酒母を投入
し、主撹拌軸を低速回転(1分間あたり2ないし10回
転が好ましい)でゆっくり回転させると、螺旋翼によっ
て固形物である蒸米を切り返しつつ下部に堆積した蒸米
をゆっくりと上部に押し上げ、切羽根によって仕込槽真
ん中部分の蒸米が切り崩され、その結果、槽上部の蒸米
は中心部付近から下部に引き込まれ、さらにパドル翼に
よって外側に押しやられた後、螺旋翼によって押し上げ
られる。このようにして、蒸米粒を激しく壊さないよう
に手作業の荒櫂操作に近い状態で撹拌混合が行われる。
やがて、麹によって蒸米が溶けて液化、糖化が進むと、
螺旋翼とパドル翼と切羽根による上記した作用により、
もろみの撹拌混合が行われる。そして、さらに液化が進
むと、主撹拌軸の回転速度はやや速められ(1分間あた
り8ないし20回転程度)、主としてパドル翼と螺旋翼
によって液の流動撹拌混合が行われる。なお、上記撹拌
混合中においては、外套内を流通する流体と仕込槽内原
料とのの熱交換により、適正な品温管理が行われる。か
くして、固形物の多い状態での切り返し混合と、液化物
の多い状態での流動混合が効率よくしかも良好な品温管
理状態のもとで行われ、優れた品質の製品を得ることが
できる。
[Function] Into the raw material charging tank, charge the charging water, koji rice (to which liquefaction enzyme and saccharifying enzyme are added as necessary), steamed rice and sake mother, and rotate the main stirring shaft at a low speed (2 to 10 rotations per minute). When rotating slowly, the steamed rice, which is a solid substance, is turned up by the spiral wings, and the steamed rice deposited at the bottom is slowly pushed up to the upper part. The steamed rice in the upper part is drawn downward from the vicinity of the center part, further pushed outward by paddle blades, and then pushed up by spiral blades. In this way, the stirring and mixing is performed in a state close to the manual rough paddle operation so as not to violate the steamed rice grains.
Eventually, when the steamed rice is melted by koji and liquefaction and saccharification progress,
By the above-mentioned action by the spiral wing, paddle wing and face,
The moromi is stirred and mixed. When the liquefaction further proceeds, the rotation speed of the main stirring shaft is slightly increased (about 8 to 20 rotations per minute), and the liquid is stirred and mixed mainly by the paddle blade and the spiral blade. During the stirring and mixing, appropriate product temperature control is performed by heat exchange between the fluid flowing in the mantle and the raw material in the preparation tank. Thus, the reciprocal mixing in a state with a large amount of solids and the fluid mixing in a state with a large amount of liquefied matter are efficiently performed under a good temperature control state, and a product of excellent quality can be obtained.

【0008】[0008]

【実施例】以下に本発明の実施例を図1を参照しながら
説明する。図1(a)において、1は原料仕込槽、2
a、2bはそれぞれ胴部、底部に設けた外套である。3
a、3bは、それぞれ外套2aへの冷熱媒体(冷水、温
水または蒸気)の供給口、排出口、4a、4bは、それ
ぞれ外套2bへの冷熱媒体(冷水、温水または蒸気)の
供給口、排出口である。本実施例においては、胴部外套
2aと底部外套2bは各々別体に原料仕込槽1の本体に
取り付けられているので、互いに連通することはない。
従って、例えば、胴部外套2aには冷媒を供給し、底部
外套2bには熱媒を供給することで、胴部の内容液の冷
却と底部の内容液の加熱が同時に、または単独で行える
という操作が可能となり、より適正且つ精密な品温管理
が行えるという利点がある。もちろん、2a、2bに上
記とは逆に冷熱媒体を供給してもよい。また、上記のよ
うな精密な品温管理が不要な場合は、胴部外套2aと底
部外套2bを一体として原料仕込槽1の本体に取り付け
てもよい。原料仕込槽1上部には原料投入口5を設け、
底部中央には処理液排出口6を設けている。
An embodiment of the present invention will be described below with reference to FIG. In FIG. 1A, reference numeral 1 denotes a raw material charging tank;
Reference numerals a and 2b denote jackets provided on the trunk and the bottom, respectively. 3
a, 3b are supply and discharge ports of a cooling medium (cold water, hot water or steam) to the mantle 2a, and 4a and 4b are supply and discharge ports of a cooling medium (cold water, hot water or steam) to the mantle 2b, respectively. Exit. In the present embodiment, since the body jacket 2a and the bottom jacket 2b are separately attached to the main body of the raw material charging tank 1, they do not communicate with each other.
Therefore, for example, by supplying a coolant to the body jacket 2a and supplying a heat medium to the bottom mantle 2b, it is possible to cool the content liquid of the body part and heat the content liquid of the bottom part simultaneously or independently. Operation becomes possible, and there is an advantage that more appropriate and precise product temperature management can be performed. Of course, a cooling medium may be supplied to 2a and 2b in the opposite manner. When the precise temperature control as described above is unnecessary, the body jacket 2a and the bottom jacket 2b may be integrally attached to the main body of the raw material charging tank 1. In the upper part of the raw material charging tank 1, a raw material inlet 5 is provided.
A processing liquid outlet 6 is provided at the center of the bottom.

【0009】原料仕込槽1の中心部鉛直方向には回転自
在の主撹拌軸7を配し、該主撹拌軸7は原料仕込槽1の
上部に設置した無段変速駆動装置8と連結されている。
原料仕込槽1の内面に近接して設けた螺旋状に形成され
た螺旋翼9は、上記主撹拌軸7から半径方向に延設した
複数の支持腕10a、10b、10cと接続されてい
る。この螺旋翼9の接続方法は、図1(a)においては
U字状のボルトを用いたが、これに限定されるものでは
なく、他の接続方法、例えば螺旋翼9と支持腕10a、
10b、10cを溶接してもよい。この螺旋翼9は仕込
槽1の内面に沿って略180°にわたって設置されてい
る。すなわち、支持腕10aから螺旋を巻き始め、10
cで巻き終わっているのである(平面図である図3参
照)。また、この螺旋翼9は略360°にわたって巻か
れてもよい。さらに、支持腕10cから反対方向に延設
させた腕11と支持腕10aに切羽根12を固定し、主
撹拌軸7の下端部にパドル翼13が固定されている。本
実施例におけるパドル翼13は2枚であるが、4枚でも
よい。また、本実施例におけるパドル翼は傾斜パドル翼
としたが、この形状に限定されるものではなく、傾斜し
ない通常のパドル翼でもよい。14は排出弁、15は温
度計である。
A rotatable main stirring shaft 7 is disposed in the center of the raw material charging tank 1 in a vertical direction, and the main stirring shaft 7 is connected to a continuously variable transmission driving device 8 installed above the raw material charging tank 1. I have.
A spiral blade 9 formed in a spiral shape and provided near the inner surface of the raw material charging tank 1 is connected to a plurality of support arms 10a, 10b, and 10c extending from the main stirring shaft 7 in the radial direction. Although the U-shaped bolt is used in FIG. 1A for the method of connecting the spiral blade 9, the present invention is not limited to this, and other connection methods, for example, the spiral blade 9 and the support arm 10 a,
10b and 10c may be welded. The spiral blade 9 is installed along the inner surface of the charging tank 1 over approximately 180 °. That is, the spiral starts to be wound from the support arm 10a.
The winding is finished at c (see FIG. 3 which is a plan view). Further, the spiral blade 9 may be wound over approximately 360 °. Further, a cutting blade 12 is fixed to the arm 11 and the support arm 10a extending in the opposite direction from the support arm 10c, and a paddle blade 13 is fixed to the lower end of the main stirring shaft 7. Although the number of the paddle blades 13 in this embodiment is two, four may be used. Further, the paddle blades in the present embodiment are inclined paddle blades, but are not limited to this shape, and may be ordinary paddle blades that do not tilt. 14 is a discharge valve, and 15 is a thermometer.

【0010】切羽根12の断面は図1(b)に示すよう
に、回転方向に先細り状でやや丸みをもった形状であ
る。
As shown in FIG. 1B, the cross section of the cutting blade 12 is tapered in the rotation direction and slightly rounded.

【0011】螺旋翼9は固形物の切り返し移動をスムー
ズにするが、原料を切り崩す切羽根12によりさらにそ
の効果を上げることができる。また、螺旋翼9は原料仕
込槽1の内面に近接して配されているので、原料仕込槽
1の胴部内面付近の内容物は、螺旋翼9の回転によっ
て、原料仕込槽1の胴部に沿って上部にスムーズに移動
するため、外套からの伝熱効果がよくなるという利点が
ある。また、螺旋翼9の外径は、螺旋翼9の翼幅や内容
物の物性によっても異なるが、原料仕込槽1の内径の略
70%以上あればよい。さらに、原料仕込槽1の内径の
略90%前後であれば、より効果的である。なお、螺旋
翼9は大型仕込槽の場合や強度の切り返しを必要とする
場合は、図2に示すように、図1の螺旋翼9が対面する
側とは反対側の仕込槽内面に近接するように、もう一
枚、別の螺旋翼9aを設けるのが好ましい。大型仕込槽
の場合は、主撹拌軸7、支持腕10a、10b、10
c、螺旋翼9およびピッチドパドル翼13を2重構造と
し、これらの内部に冷水または温水を通水することによ
って、原料の品温管理を良好に維持することができる。
The spiral blade 9 smoothes the turning movement of the solid material, but the effect can be further enhanced by the cutting blade 12 for cutting down the raw material. Further, since the spiral wing 9 is arranged close to the inner surface of the raw material charging tank 1, the contents near the inner surface of the trunk of the raw material charging tank 1 are rotated by the rotation of the spiral blade 9, so that the body of the raw material charging tank 1 is rotated. There is an advantage that the heat transfer effect from the mantle is improved because of the smooth movement to the upper part along. The outer diameter of the spiral blade 9 varies depending on the blade width of the spiral blade 9 and the physical properties of the contents, but it is sufficient that the outer diameter is approximately 70% or more of the inner diameter of the raw material charging tank 1. Furthermore, it is more effective if the inner diameter of the raw material charging tank 1 is approximately 90%. When the spiral blade 9 is a large charging tank or when it is necessary to switch the strength, as shown in FIG. 2, the spiral blade 9 is close to the inner surface of the charging tank opposite to the side facing the spiral blade 9 in FIG. In order to do so, it is preferable to provide another spiral wing 9a. In the case of a large charging tank, the main stirring shaft 7, the supporting arms 10a, 10b, 10
c, the spiral blade 9 and the pitched paddle blade 13 have a double structure, and by passing cold or hot water through them, it is possible to maintain good control of the material temperature of the raw material.

【0012】図3は螺旋翼9と支持腕10a、10b、
10cを上から見た平面図である。
FIG. 3 shows a spiral wing 9 and supporting arms 10a, 10b,
It is the top view which looked at 10c from the top.

【0013】この場合、切羽根12の断面は三角形とし
ている。切羽根12の断面形状は、図1(b)のように
やや丸みをもった形状でもよい。要は回転方向に先細り
状であればよいのである。
In this case, the cross section of the face 12 is triangular. The cross-sectional shape of the cutting blade 12 may be slightly rounded as shown in FIG. The point is that it only has to be tapered in the rotation direction.

【0014】[0014]

【発明の効果】本発明は上記のように構成されているの
で、次の効果を奏する。 原料中の固形物量が多い場合は、主撹拌軸を低速回
転させることで、螺旋翼と切羽根とピッチドパドル翼に
より、原料を破砕せずに切り込み、切り崩しを行い、原
料の上下移動および撹拌混合がスムーズに行われ、併せ
て外套との間での熱移動を通じて液化、糖化または醗酵
の促進のための品温管理が行われる。液化、糖化の進行
に従って液状物質が増加した場合には、主撹拌軸をやや
速く回転させることによって、主として螺旋翼とピッチ
ドパドル翼により原料の流動撹拌混合がスムーズに行わ
れ、同時に外套との間での熱移動により、一定の品温管
理のもとに良好な品質の製品を得ることができる。さら
に、外套を原料仕込槽の胴部と底部に別体に配すること
で、より良好・精密な品温管理が可能となる。
As described above, the present invention has the following advantages. When the amount of solids in the raw material is large, the main stirring shaft is rotated at a low speed, and the spiral blade, cutting blade, and pitched paddle blade cut and cut the raw material without crushing, and the vertical movement of the raw material and stirring and mixing are performed. It is performed smoothly, and at the same time, temperature control for promoting liquefaction, saccharification, or fermentation is performed through heat transfer with the mantle. When the liquid substance increases with the progress of liquefaction and saccharification, by rotating the main stirring shaft slightly faster, the flow stirring and mixing of the raw material is smoothly performed mainly by the spiral blade and the pitched paddle blade, and at the same time, between the outer jacket By means of heat transfer, a product of good quality can be obtained under constant temperature control. Furthermore, by arranging the mantle separately on the body part and the bottom part of the raw material charging tank, better and more precise product temperature control becomes possible.

【0015】 本発明の装置は、酒類のみならず、穀
物を原料とする液化および醗酵工程を有する食品の製造
に広く適用することができる。
The apparatus of the present invention can be widely applied not only to alcoholic beverages but also to the production of foods having liquefaction and fermentation steps using grains as raw materials.

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

【図1】図1(a)は本発明の一実施例の断面図、図1
(b)は切羽根の断面図である。
FIG. 1A is a sectional view of one embodiment of the present invention, FIG.
(B) is sectional drawing of a cutting blade.

【図2】本発明の別の実施例の断面図である。FIG. 2 is a cross-sectional view of another embodiment of the present invention.

【図3】螺旋翼および支持腕を示す平面図である。FIG. 3 is a plan view showing a spiral wing and a support arm.

【図4】切り込み撹拌翼を備えた従来の撹拌装置の断面
図である。
FIG. 4 is a cross-sectional view of a conventional stirring device provided with a notch stirring blade.

【符号の説明】[Explanation of symbols]

1…原料仕込槽 2a、2b…外套 3a、4a…供給口 3b、4b…排出口 5…原料投入口 6…処理液排出口 7…主撹拌軸 8…無段変速駆動装置 9、9a…螺旋翼 10a、10b、10c…支持腕 11…腕 12…切羽根 13…パドル翼 14…排出弁 15…温度計 21…モータ 22…撹拌軸 23…切り込み撹拌翼 24…外套 DESCRIPTION OF SYMBOLS 1 ... Material supply tank 2a, 2b ... Jacket 3a, 4a ... Supply port 3b, 4b ... Discharge port 5 ... Material input port 6 ... Processing liquid discharge port 7 ... Main stirring shaft 8 ... Continuously variable speed drive 9, 9a ... Spiral Blades 10a, 10b, 10c Support arm 11 Arm 12 Cutting blade 13 Paddle blade 14 Discharge valve 15 Thermometer 21 Motor 22 Stirring shaft 23 Cutting stirrer blade 24 Jacket

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C12G 3/00 Continuation of front page (58) Field surveyed (Int.Cl. 7 , DB name) C12G 3/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 胴部と底部に外套を有する筒状の原料仕
込槽の中心部鉛直方向に回転自在に主攪拌軸を配し、上
記原料仕込槽の内面に近接して螺旋状に形成された螺旋
翼を配し、上記主攪拌軸から半径方向に延設した複数の
支持腕に該螺旋翼を接続し、主攪拌軸下端部にパドル翼
を固定し、さらに、主攪拌軸と螺旋翼との間において鉛
直方向に原料仕込槽内の原料を切り崩すための切羽根を
設けたことを特徴とするもろみの仕込槽
1. A main stirring shaft is rotatably arranged in a central portion of a cylindrical raw material charging tank having a shell at a body portion and a bottom portion so as to be rotatable in a vertical direction, and is formed in a spiral shape close to an inner surface of the raw material charging tank. Helical blades are connected, the spiral blades are connected to a plurality of support arms extending radially from the main stirring shaft, paddle blades are fixed to the lower end of the main stirring shaft, and the main stirring shaft and the spiral blades are further fixed. A moromi mashing tank provided with cutting blades for cutting down the raw material in the mashing tank in the vertical direction between the mashing tank and the mash .
【請求項2】 切羽根の断面形状が回転方向に先細り状
であることを特徴とする請求項1記載のもろみの仕込
2. The mash filling according to claim 1, wherein the cross-sectional shape of the cutting blade is tapered in the rotation direction.
Tank .
JP12103594A 1994-06-02 1994-06-02 Moromi mashing tank Expired - Lifetime JP3056947B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12103594A JP3056947B2 (en) 1994-06-02 1994-06-02 Moromi mashing tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12103594A JP3056947B2 (en) 1994-06-02 1994-06-02 Moromi mashing tank

Publications (2)

Publication Number Publication Date
JPH07322871A JPH07322871A (en) 1995-12-12
JP3056947B2 true JP3056947B2 (en) 2000-06-26

Family

ID=14801213

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12103594A Expired - Lifetime JP3056947B2 (en) 1994-06-02 1994-06-02 Moromi mashing tank

Country Status (1)

Country Link
JP (1) JP3056947B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4681131B2 (en) * 2001-01-26 2011-05-11 宝ホールディングス株式会社 Liquor production equipment
JP4979158B2 (en) * 2001-03-28 2012-07-18 日本化学機械製造株式会社 Stirrer
KR100783083B1 (en) * 2006-09-11 2007-12-07 권상동 A agitator for treating organic waste
CN106422864A (en) * 2016-09-18 2017-02-22 上海超金节能科技股份有限公司 Surrounding flow stirring kettle
CN106947692B (en) * 2017-04-06 2023-03-31 扬州日兴生物科技股份有限公司 Reaction unit is used in preparation of biotransformation fermentation glucosamine
CN107509810A (en) * 2017-07-21 2017-12-26 广东金维牛奶有限公司 Milk beverage production fermentation tank
CN114075495A (en) * 2020-08-18 2022-02-22 盘锦大工碱蓬生物科技有限公司 Suaeda salsa wine and brewing process thereof

Also Published As

Publication number Publication date
JPH07322871A (en) 1995-12-12

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