JPS6233869B2 - - Google Patents

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Publication number
JPS6233869B2
JPS6233869B2 JP58017884A JP1788483A JPS6233869B2 JP S6233869 B2 JPS6233869 B2 JP S6233869B2 JP 58017884 A JP58017884 A JP 58017884A JP 1788483 A JP1788483 A JP 1788483A JP S6233869 B2 JPS6233869 B2 JP S6233869B2
Authority
JP
Japan
Prior art keywords
mash
tank
tank body
stirring
air
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
JP58017884A
Other languages
Japanese (ja)
Other versions
JPS59143585A (en
Inventor
Hidekazu Yamazaki
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.)
MARUKIN SHOYU KK
Original Assignee
MARUKIN SHOYU 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 MARUKIN SHOYU KK filed Critical MARUKIN SHOYU KK
Priority to JP58017884A priority Critical patent/JPS59143585A/en
Publication of JPS59143585A publication Critical patent/JPS59143585A/en
Publication of JPS6233869B2 publication Critical patent/JPS6233869B2/ja
Granted legal-status Critical Current

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  • Soy Sauces And Products Related Thereto (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Description

【発明の詳細な説明】 本発明は回転式もろみ醗酵タンクに関する。[Detailed description of the invention] The present invention relates to a rotary mash fermentation tank.

もろみ醗酵に際し、当初タンク内に投入された
麹は吸水性が良好でない上に液体との比重差が大
きく液面に浮き、しかも固液の容積比も固体が多
いなどの理由により、混合撹拌が容易でない。特
に醗酵過程の進行により粘度が増加してくると、
一層容易でなくなる。
During moromi fermentation, the koji initially put into the tank does not have good water absorption, has a large difference in specific gravity from the liquid, and floats on the liquid surface, and the volume ratio of solid to liquid is high, making mixing and stirring difficult. It's not easy. Especially as the viscosity increases as the fermentation process progresses,
It becomes even less easy.

従来もろみ醗酵過程に於ける混合撹拌手段とし
て、混合撹拌と酸素供給を同時に行うような空気
吹込み法が一般に採用されているが、このような
空気吹込み法の適用のみでは、混合撹拌難度の高
いもろみを充分良好に混合撹拌することは難かし
いのみならず、空気の吹込量(酸素の供給量)と
混合撹拌効果は平衡関係にあるため、醗酵過程の
時々で望まれるような、例えば良好な混合撹拌効
果を保持したままで酸素の供給量に制限を加える
というような醗酵状況に見合つた最適条件を作出
することはできず、最適条件のある部分を犠牲に
せざるを得ない欠点があつた。この場合、空気の
吹込みとは別に撹拌翼などを用いてもろみの混合
撹拌を行うことが考えられるが、撹拌翼を速く回
転するともろみが泥状になつて醗酵に悪影響を与
えることになり、一方低速回転すると混合撹拌効
果が期待できなくなり、撹拌翼の併設は好ましい
解決策でない。
Conventionally, as a mixing and stirring means in the moromi fermentation process, an air blowing method that performs mixing and stirring and oxygen supply at the same time has been generally adopted. Not only is it difficult to mix and stir a high-quality mash, but also there is an equilibrium relationship between the amount of air blown (oxygen supply amount) and the mixing and stirring effect. It is not possible to create optimal conditions that match the fermentation situation, such as limiting the amount of oxygen supplied while maintaining a good mixing and stirring effect, and there is a drawback that certain parts of the optimal conditions must be sacrificed. Ta. In this case, it may be possible to mix and stir the mash using a stirring blade or the like in addition to blowing air, but if the stirring blade is rotated too quickly, the mash will become muddy and have a negative impact on fermentation. On the other hand, if it rotates at a low speed, the mixing and stirring effect cannot be expected, and the provision of stirring blades is not a preferable solution.

本発明はこのような問題を一掃することを目的
として鋭意研究を重ねた結果、球状密閉型であつ
て内面に撹拌部材を固設した醗酵タンクを低速回
転するときは、もろみを泥状化することなしに良
好な混合撹拌効果が得られることを見出し、茲に
本発明を完成するに至つたものである。
The present invention was developed as a result of intensive research aimed at eliminating such problems.When rotating a fermentation tank, which is a spherical sealed type and has a stirring member fixed to its inner surface, at low speed, the mash is turned into sludge. It was discovered that a good mixing and stirring effect can be obtained without any problems, and this led to the completion of the present invention.

即ち本発明は、中空の水平横軸に於て回転自在
に軸架されたタンク本体と、該本体を低速回転す
るための回転駆動装置と、もろみの加温、冷却装
置と、更にもろみ内への空気吹込み装置を具備
し、上記タンク本体は略々球状密閉型であつて、
内面の適宜の個所に撹拌部材が備えられ、更にタ
ンク本体に、上記水平横軸の中空部を通じて、上
記加温、冷却装置としての配管と、上記空気吹込
み装置としての配管が施されていることを特徴と
する回転式もろみ醗酵タンクに係る。
That is, the present invention provides a tank body that is rotatably mounted on a hollow horizontal axis, a rotary drive device for rotating the main body at low speed, a device for heating and cooling the mash, and a tank body that is rotatably mounted on a hollow horizontal axis. The tank body is of a substantially spherical closed type,
Stirring members are provided at appropriate locations on the inner surface, and piping for the heating and cooling device and piping for the air blowing device are provided in the tank body through the hollow portion of the horizontal horizontal shaft. This invention relates to a rotary mash fermentation tank characterized by the following.

以下に本発明の実施例を添附図面にもとづき説
明すると次の通りである。
Embodiments of the present invention will be described below based on the accompanying drawings.

図に於て、1は中心を挾さんで左右に対向する
中空の水平横軸2,2に於て軸受け3,3に回転
自在に軸架された球状密閉型のタンク本体であつ
て、該タンク本体1は頂部に原料投入口1aを底
部に製品排出口1bを有し、通常運転時には、之
等は蓋体4a,4bにより密閉されている。タン
ク本体1としては、第1〜3図に示された球状の
ものに加え、第4図に示された上下部裁断の略々
球状のものであつてもよい。
In the figure, reference numeral 1 denotes a spherical sealed tank body rotatably mounted on bearings 3, 3 on hollow horizontal horizontal shafts 2, 2 facing left and right across the center. The tank body 1 has a raw material input port 1a at the top and a product discharge port 1b at the bottom, which are sealed by lids 4a and 4b during normal operation. In addition to the spherical tank body 1 shown in FIGS. 1 to 3, the tank body 1 may have a substantially spherical shape with upper and lower sections shown in FIG. 4.

5はタンク本体1の内面に固設されたもろみ混
合撹拌用の撹拌部材であつて、撹拌部材5として
図にはブレード型のものが示されているが、その
他ピン型などであつてもよい。またその固設位置
及び固設数も任意であり、実験的に適宜選定すれ
ばよい。図には撹拌部材5を半球部ごとに上下左
右の4個所、都合8ケ所に設けた場合が示されて
いる。
Reference numeral 5 denotes a stirring member for mixing and stirring the mash, which is fixedly installed on the inner surface of the tank body 1. Although a blade-type stirring member 5 is shown in the figure, other shapes such as a pin-type may be used as the stirring member 5. . Further, the fixed position and the number of fixed parts are also arbitrary, and may be appropriately selected experimentally. The figure shows a case where stirring members 5 are provided at four locations on the top, bottom, left and right of each hemisphere, a total of eight locations.

6はタンク本体1を低速回転するための回転駆
動装置であつて、該装置6としては公知の各種の
形式のものを採用でき、図には横軸2上に固設さ
れたスプロケツト6aと、モータ(図示せず)よ
りの回転をスプロケツト6aに伝達するチエン6
bからなる方式のものが示されている。
Reference numeral 6 denotes a rotary drive device for rotating the tank body 1 at a low speed, and various types of known types can be adopted as the device 6. The figure shows a sprocket 6a fixedly installed on the horizontal shaft 2, A chain 6 that transmits rotation from a motor (not shown) to a sprocket 6a.
A system consisting of b is shown.

7は空気吹込み装置を構成するように、一方の
横軸2(第1図に於て右側)の中空部を通じてタ
ンク本体1内に配管された空気及び/又は水(塩
水を含む)の供給管で、該供給管7の内端部はタ
ンク本体1の中心から底部へ延出され、この延出
部7a下端の側口7bより空気及び/又は水を供
給し得るようになつている。一方外端部はタンク
外で2方に分岐され、一方分岐部71は空気の加
圧供給部(図示せず)に、また他方分岐部72は
水の加圧供給部(図示せず)に、それぞれ連絡さ
れている。
7 is a supply of air and/or water (including salt water) piped into the tank body 1 through the hollow part of one horizontal shaft 2 (on the right side in FIG. 1) so as to constitute an air blowing device. The inner end of the supply pipe 7 extends from the center of the tank body 1 to the bottom, and air and/or water can be supplied from a side port 7b at the lower end of the extended part 7a. On the other hand, the outer end is branched into two directions outside the tank, with one branch 71 connected to a pressurized air supply (not shown), and the other branch 72 connected to a pressurized water supply (not shown). , have been contacted respectively.

8は供給管7内を通つてタンク本体1内の気相
部まで配管された排気管で、内端は気相部に開口
され、この開口8aを通じて、気相部内の気体を
空気の吹込みにつれタンク外に排出する。
Reference numeral 8 denotes an exhaust pipe that passes through the supply pipe 7 and reaches the gas phase in the tank body 1, and its inner end is opened to the gas phase, and the gas in the gas phase is blown into the gas phase through this opening 8a. As time passes, it will be discharged out of the tank.

9は他方の横軸2(第1図に於て左側)の中空
部を通じてタンク内に配管された2重管構造の加
熱(又は冷却)用流体循環管で、流体は循環管9
の往路(外管部91)を通りタンク中心部に至
り、ここよりバイパス93を経てタンクの底部中
央に至り、上昇して復路(内管部92)を通じタ
ンク外へ導出され、加熱(又は冷却)されて後再
び往路へ戻されるようになつている。この循環管
9が加熱、冷却装置を構成している。
Reference numeral 9 denotes a heating (or cooling) fluid circulation pipe with a double pipe structure that is piped into the tank through the hollow part of the other horizontal shaft 2 (on the left side in Fig. 1), and the fluid is passed through the circulation pipe 9.
It passes through the outgoing route (outer pipe part 91) to reach the center of the tank, from here it passes through the bypass 93 to reach the center of the bottom of the tank, rises, and is led out of the tank through the return route (inner pipe part 92), where it is heated (or cooled). ) and then returned to the outbound route. This circulation pipe 9 constitutes a heating and cooling device.

10は横軸2の中空部内周面を回転面、またこ
れに挿通された管7及び9の外周面を固定面とし
て、之等の間を液封する液封機構であつて、液封
機構10としては公知の各種形式のものを採用で
きる。
Reference numeral 10 denotes a liquid sealing mechanism which uses the inner circumferential surface of the hollow part of the horizontal shaft 2 as a rotating surface and the outer circumferential surfaces of the tubes 7 and 9 inserted therein as fixed surfaces, and seals liquid between the two. As 10, various types of known types can be adopted.

本発明醗酵タンクは上述の如き構造を有し、図
示の状態で球状のタンク本体1を回転駆動装置6
により低速回転することにより、本体1の内面に
固設した撹拌部材5でもつてもろみの混合撹拌を
行い得るものである。この際本発明に於ては、特
にタンク本体1を球状となすと共にその内面に撹
拌部材5を固設したので、タンク全体が撹拌機能
を発揮することに加え、タンク内もろみが全周囲
から混合撹拌力を受けることになり、その結果こ
れが低速回転であるに拘わらず極めて高度の混合
撹拌効果が得られ、混合撹拌難度の高い投入初期
のもろみ原料であつてもこれを充分良好に混合撹
拌し得る。しかもこれが低速回転であるためにも
ろみを泥状化し、以後の醗酵に悪影響を与えるよ
うな虞れも全く有しないものである。ちなみにタ
ンクの回転数は、タンクの規模やもろみの醗酵の
進行状況などによつても左右されるが、通常1分
間当り10回転以下程度の極く低速回転に止どめる
べきであり、このうちでも特に1〜3回転程度の
低速回転が好結果が得られる。もろみの混合撹拌
は、醗酵の全過程を通じて必要とするものでな
く、醗酵の進行状況によつては一時停止すること
が好ましい場合があり、このような場合にはタン
ク本体1の回転が停止される。
The fermentation tank of the present invention has the above-described structure, and the spherical tank body 1 is rotated by the rotation drive device 6 in the state shown in the figure.
By rotating at a low speed, even the stirring member 5 fixed to the inner surface of the main body 1 can mix and stir the mash. At this time, in the present invention, in particular, the tank body 1 is made spherical and the stirring member 5 is fixed on its inner surface, so that in addition to the entire tank exhibiting a stirring function, the mash in the tank is mixed from all around. As a result, even though the rotation speed is low, an extremely high mixing and stirring effect can be obtained, and even if it is a mash raw material that is difficult to mix and stir at the initial stage of addition, it can be mixed and stirred well. obtain. Furthermore, since this rotation is performed at a low speed, there is no risk of turning the mash into sludge and adversely affecting subsequent fermentation. By the way, the rotation speed of the tank depends on the size of the tank and the progress of fermentation of the mash, but it should normally be kept to an extremely low rotation speed of about 10 revolutions per minute or less. Among these, particularly good results can be obtained with low speed rotation of about 1 to 3 rotations. Mixing and stirring of the mash is not necessary throughout the entire fermentation process, and depending on the progress of fermentation, it may be preferable to temporarily stop the mixing, and in such cases, the rotation of the tank body 1 is stopped. Ru.

更にもろみを所定の溶存酸素量に保持するため
に、空気吹込み装置としての供給管7より、空気
の必要量が連続して又は断続的にもろみ内に吹込
まれ、この際同時に又は個別操作的に水(塩水を
含む)の必要量がもろみ内に供給される場合もあ
る。この空気の吹込みは、もろみの混合撹拌に寄
与するが、本発明では先に述べたように、もろみ
の混合撹拌をタンクの低速回転によつて行い得る
ような構成を採用しているので、空気の吹込み
は、醗酵過程の時々で望まれる最適の酸素溶存量
が得られるように行なえばよい。
Furthermore, in order to maintain the mash at a predetermined amount of dissolved oxygen, the required amount of air is continuously or intermittently blown into the mash through a supply pipe 7 serving as an air blowing device, and at this time, air may be blown into the mash simultaneously or individually. In some cases, the required amount of water (including brine) is supplied into the mash. This blowing of air contributes to the mixing and stirring of the mash, but as mentioned earlier, the present invention adopts a configuration in which the mash can be mixed and stirred by the slow rotation of the tank. Air may be blown in such a way as to obtain the optimum amount of dissolved oxygen desired at various times during the fermentation process.

更にもろみを所定の品温に保持するために、加
熱、冷却装置としての循環管9に、加温(又は冷
却)用流体が循環され、この循環によつて、もろ
みは醗酵過程の時々に見合つた最適の品温に保持
される。
Furthermore, in order to maintain the mash at a predetermined temperature, a heating (or cooling) fluid is circulated through a circulation pipe 9 that serves as a heating and cooling device, and through this circulation, the mash is heated at different times during the fermentation process. The product is maintained at the optimum temperature.

このように本発明に於ては、もろみの混合撹
拌、品温並びに酸素溶存量の保持を、それぞれ独
立して個別操作的に行い得るので、もろみの醗酵
過程に応じた最適条件を容易に作出でき、全過程
を通じて最適条件のもとに、もろみの醗酵熟成を
行い得られ、しかももろみの混合撹拌を必要とす
る場合には、撹拌部材付の球状タンクの低速回転
によつて、もろみを泥状化するなどの危険性なし
に充分良好に混合撹拌でき、全体としてこの種醗
酵タンクの性能を格段と向上し得る特徴を有す
る。
In this way, in the present invention, the mixing and stirring of the mash, the maintenance of the product temperature, and the amount of dissolved oxygen can be performed independently and individually, so it is easy to create the optimal conditions according to the fermentation process of the mash. The mash can be fermented and matured under optimal conditions throughout the entire process, and if mixing and stirring of the mash is required, the mash can be mixed into a slurry by rotating at low speed in a spherical tank equipped with a stirring member. It has the characteristics that it can be mixed and stirred sufficiently well without the risk of oxidation, and the performance of this seed fermentation tank as a whole can be greatly improved.

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

第1図は本発明の一実施例を示す中央縦断正面
図、第2図は同横断平面図、第3図は同縦断側面
図、第4図は本発明の実施の他例を示す中央縦断
正面図である。 図に於て、1はタンク本体、2は横軸、3は軸
受、4a,4bは蓋体、5は撹拌部材、6は回転
駆動装置、7は供給管、8は排気管、9は循環
管、10は液封機構である。
FIG. 1 is a front view in central longitudinal section showing one embodiment of the present invention, FIG. 2 is a cross-sectional plan view thereof, FIG. 3 is a side view in longitudinal section thereof, and FIG. 4 is a longitudinal cross-sectional view showing another embodiment of the present invention. It is a front view. In the figure, 1 is the tank body, 2 is the horizontal axis, 3 is the bearing, 4a, 4b are the lids, 5 is the stirring member, 6 is the rotary drive device, 7 is the supply pipe, 8 is the exhaust pipe, 9 is the circulation The tube 10 is a liquid sealing mechanism.

Claims (1)

【特許請求の範囲】[Claims] 1 中空の水平横軸に於て回転自在に軸架された
タンク本体と、該本体を低速回転するための回転
駆動装置と、もろみの加温、冷却装置と、更にも
ろみ内への空気吹込み装置を具備し、上記タンク
本体は略々球状密閉型であつて、内面の適宜の個
所に撹拌部材が備えられ、更にタンク本体に、上
記水平横軸の中空部を通じて、上記加温、冷却装
置としての配管と、上記空気吹込み装置としての
配管が施されていることを特徴とする回転式もろ
み醗酵タンク。
1. A tank body rotatably mounted on a hollow horizontal axis, a rotary drive device for rotating the main body at low speed, a heating and cooling device for the mash, and a blowing of air into the mash. The tank body is of a substantially spherical closed type, and stirring members are provided at appropriate locations on the inner surface, and the heating and cooling device is connected to the tank body through the hollow part of the horizontal horizontal axis. A rotary mash fermentation tank characterized in that it is equipped with piping as an air blowing device and piping as the air blowing device.
JP58017884A 1983-02-04 1983-02-04 Rotary tank for fermentation of moromi (unrefined soy) Granted JPS59143585A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58017884A JPS59143585A (en) 1983-02-04 1983-02-04 Rotary tank for fermentation of moromi (unrefined soy)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58017884A JPS59143585A (en) 1983-02-04 1983-02-04 Rotary tank for fermentation of moromi (unrefined soy)

Publications (2)

Publication Number Publication Date
JPS59143585A JPS59143585A (en) 1984-08-17
JPS6233869B2 true JPS6233869B2 (en) 1987-07-23

Family

ID=11956127

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58017884A Granted JPS59143585A (en) 1983-02-04 1983-02-04 Rotary tank for fermentation of moromi (unrefined soy)

Country Status (1)

Country Link
JP (1) JPS59143585A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH035456U (en) * 1989-06-02 1991-01-21

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE202004006610U1 (en) * 2004-04-24 2005-09-08 Infors Ag fermenter

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4949200U (en) * 1972-08-08 1974-04-30
JPS51128497A (en) * 1975-05-01 1976-11-09 Nagasaki Shoyu Miso Kogyo Kyodo Kumiai Method for blending of the feeding raw materials on brewing soy

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH035456U (en) * 1989-06-02 1991-01-21

Also Published As

Publication number Publication date
JPS59143585A (en) 1984-08-17

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