JPH03201973A - Fermentation with saccharification - Google Patents

Fermentation with saccharification

Info

Publication number
JPH03201973A
JPH03201973A JP1338732A JP33873289A JPH03201973A JP H03201973 A JPH03201973 A JP H03201973A JP 1338732 A JP1338732 A JP 1338732A JP 33873289 A JP33873289 A JP 33873289A JP H03201973 A JPH03201973 A JP H03201973A
Authority
JP
Japan
Prior art keywords
saccharification
materials
tank
raw materials
fermentation
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
JP1338732A
Other languages
Japanese (ja)
Inventor
Akira Osawa
大沢 旭
Shigehiro Sato
繁博 佐藤
Akihito Suzuki
章仁 鈴木
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP1338732A priority Critical patent/JPH03201973A/en
Publication of JPH03201973A publication Critical patent/JPH03201973A/en
Pending legal-status Critical Current

Links

Landscapes

  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Abstract

PURPOSE:To accomplish the process simplification for fermentation by saccharification through such processes that the first tank is charged with raw materials followed by transferring the materials into plural tanks arranged in parallel, and the materials are left to stay for a specified time in each of the tanks, thereby producing saccharified unrefined soy in a simple manner. CONSTITUTION:Raw materials heat-treated in a boiler 131 are transferred through a pump 121 into a tank 101. Powdery sub-materials in vessels 112-117 and liquid sub-materials in a vessel 111 are also fed into the tank 101, and the raw materials thus combined are agitated and held for a specified time, and then transferred, using a pump 123, into saccharification tanks 102-106 where the materials are held again for a specified time and saccharified, thus obtaining the objective saccharified unrefined soy.

Description

【発明の詳細な説明】 〔産梁1・、の利用分野] 本発明は原料の勧化発酵に関し、特に食酢の原料勧化発
酵方法に有効に適用しうる糖化発酵方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of Sanryo 1.] The present invention relates to the fermentation of raw materials, and particularly to a saccharification and fermentation method that can be effectively applied to the fermentation method of raw materials for vinegar.

〔従来の技術〕[Conventional technology]

】な酢公造において穀物を原料とし、これに麹、水その
他副原斜を加えて助化醪とするには、これらn;CLl
を1つのタンクに滞留させて1〜数日かかるため、その
日数分の複数のタンクを用意し、jハツチずつ日時をず
らして原料及び副原料を仕込んでいる。これは同時に仕
込んで一度に大量の糖化醪ができ、後工程の待ち時間が
できてしまうことを避け、かつ、品質の均一化を保つた
めでもある。
] In vinegar production, grains are used as raw materials, and in order to make sukekamomi by adding koji, water, and other secondary ingredients, these n; CLl are necessary.
Because it takes one to several days to retain the raw materials and auxiliary materials in one tank, multiple tanks are prepared for that number of days, and raw materials and auxiliary materials are charged into each batch at staggered dates and times. This is to avoid having to prepare a large amount of saccharified moromi at once, which would require waiting time for the subsequent process, and to maintain uniform quality.

従来の勧化発酵工程を第2図によって説明する。The conventional fermentation process will be explained with reference to FIG.

原料(よ蒸煮缶231で処理された後、ポンプ221に
よって発酵糖化タンク(以下糖化タンク)201〜20
6に運ばれる。このとき切換バルブ261〜265を操
作すること1ζより、粘化タンク201〜206を選定
する。同様に容器212〜217中の粉体状の副原料は
重力により容器234を経て、また容器211中の液体
状のものはポンプ222によって原料が投入された糖化
タンク201〜206に供給される。この場合も切換バ
ルブ241〜245、及び251〜255を操作するた
とにより糖化タンクを選定する。
After the raw materials are processed in the steamer 231, they are transferred to fermentation and saccharification tanks (hereinafter referred to as saccharification tanks) 201 to 20 by the pump 221.
6. At this time, the viscosifying tanks 201 to 206 are selected by operating the switching valves 261 to 265. Similarly, powdered auxiliary raw materials in containers 212 to 217 are fed by gravity through container 234, and liquid materials in container 211 are supplied by pump 222 to saccharification tanks 201 to 206 into which the raw materials have been introduced. In this case as well, the saccharification tank is selected by operating the switching valves 241-245 and 251-255.

原料及び副原料を投入した後、攪拌機271〜276に
よってこれらの原料は均一に攪拌され、その後約1〜7
日間糖化発酵させられる。
After adding the raw materials and auxiliary raw materials, these raw materials are uniformly stirred by the stirrers 271 to 276, and then approximately 1 to 7
It is saccharified and fermented for several days.

以上の操作を糖化タンク201から206まで順次日時
をずらして行なう。糖化発酵の終了した原ネ4、すなわ
ち糖化醪はポンプ223により次工程へ送られる。
The above operations are performed sequentially for the saccharification tanks 201 to 206 at different dates and times. The raw material 4 that has undergone saccharification and fermentation, that is, the saccharified mash, is sent to the next step by the pump 223.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

従来の方法では各糖化タンクに直接原料、副原料を供給
することとなり、タンク選定のための配管が複雑となり
、また、バルブの切換え等の制御系も複雑となる。
In the conventional method, raw materials and auxiliary raw materials are directly supplied to each saccharification tank, which complicates piping for tank selection and also complicates control systems such as valve switching.

さらに1つのタンクで原料の糖化発酵工程の全てをまか
なうため、糖化発酵工程の進行に応じて昇温や冷却が必
要な場合、各タンクにそれぞれ昇温、冷却の機能をもた
せる必要があった。
Furthermore, since one tank covers all of the saccharification and fermentation processes for the raw materials, each tank needed to have its own heating and cooling functions if it was necessary to raise or cool the temperature as the saccharification and fermentation process progressed.

本発明は上記技術水型に鑑み、原料、副原料の供給配管
及び糖化醪の払い出し配管を大幅に簡略化でき、かつ制
御手段も簡単なものにすることができる糖化発酵方法を
提供しようとするものである。
In view of the above technology, the present invention aims to provide a saccharification and fermentation method that can greatly simplify the supply piping for raw materials and auxiliary raw materials and the discharging piping for the saccharified mash, as well as simplifying the control means. It is something.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は原料を糖化発酵するに当り、原料を最初のタン
クに受入れてから、その後に並列に配置した複数個のタ
ンクに内容物を移動させ、それぞれのタンクで一定時間
滞留させてから糖化醪を得るようにした糖化、発酵方法
である。
In the present invention, when raw materials are saccharified and fermented, the raw materials are received in a first tank, and then the contents are transferred to multiple tanks arranged in parallel, and the contents are left in each tank for a certain period of time before being processed into saccharification and fermentation. This is a saccharification and fermentation method designed to obtain

〔作用〕[Effect]

従来は同一タンクで仕込みから発酵、熟成まで全てを行
なっていたが、原料及び副原料の投入、糖化発酵をそれ
ぞれのタンクに分担させることにより、すべてのタンク
に必要であった攪拌機)11!びに原料、副原料供給配
管を最初のタンクのみに取りつける等各タンクの付属品
、配管を大幅に緘らすことができ、全体として糖化発酵
工程が合理化される。
Traditionally, everything from preparation to fermentation and aging was done in the same tank, but by having each tank share the input of raw materials and auxiliary materials, as well as saccharification and fermentation, a stirrer was required in all tanks) 11! In addition, the accessories and piping for each tank can be significantly reduced, such as by attaching the raw material and auxiliary raw material supply piping only to the first tank, and the saccharification and fermentation process as a whole is streamlined.

〔実施例〕〔Example〕

本発明糖化発酵方法の一実施例を第1図によって説明す
る。
An embodiment of the saccharification and fermentation method of the present invention will be explained with reference to FIG.

原料は蒸煮缶131で熱処理された後、ポンプ121に
より糖化タンク101に運ばれる。
The raw material is heat-treated in the steamer 131 and then transported to the saccharification tank 101 by the pump 121.

同様に容器112〜11?中の粉体状副原料は重力によ
り容器134を経て、また容器111の液体状のものは
ポンプ122によって糖化タンク+01に供給される。
Similarly, containers 112-11? The powdered auxiliary raw material inside passes through the container 134 by gravity, and the liquid material in the container 111 is supplied to the saccharification tank +01 by the pump 122.

原料と副原料は攪拌1幾181により攪拌され、一定時
間ホールドされる。その後、ポンプ123により糖化タ
ンク102〜106に運ばれる。このとき切換バルブ1
/ll−144を操作することにより、糖化タンク10
2〜106を選定する。糖化の終了した原料、すなわち
糖化醪は切換バルブ151〜+5/lを経てポンプ12
4により次工程へ送られる。
The raw material and the auxiliary raw material are stirred by stirring 181 and held for a certain period of time. Thereafter, it is transported to the saccharification tanks 102 to 106 by the pump 123. At this time, switching valve 1
/ll-144, the saccharification tank 10
Select 2 to 106. The raw material that has been saccharified, that is, the saccharified moromi, passes through the switching valve 151 to +5/l to the pump 12.
4, it is sent to the next process.

〔発明の効果〕〔Effect of the invention〕

本発明による方法により、糖化発酵工程での機能を損な
うことなく、原料、副原料の搬送システムの簡略化を行
なうことができる。また、昇温、冷却及び攪拌機能が必
要なのは副原料投入後数時間であり、その後は静置させ
ておくだけでJ)るため、本発明においては副原料を投
入するタンクにのみしか昇温、冷却及び攪拌装置を設け
る必要がないので、攪拌機、昇温、冷却装置が必要な勧
化タンクは最初の一基のみとなることにより、タンクの
洗浄が容易となり、コストの低減も図れる。
By the method according to the present invention, the transportation system for raw materials and auxiliary raw materials can be simplified without impairing the functions in the saccharification and fermentation process. In addition, the temperature raising, cooling, and stirring functions are only required for several hours after the addition of the auxiliary materials, and after that, the temperature can only be increased in the tank into which the auxiliary materials are input. Since there is no need to provide a cooling and stirring device, only the first tank requires a stirring device, temperature raising device, and cooling device, making it easier to clean the tank and reducing costs.

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

第1図は本発明の一実施例の説明図、第2図は従来の糖
化発酵方法の一態様の説明図である。
FIG. 1 is an explanatory diagram of an embodiment of the present invention, and FIG. 2 is an explanatory diagram of an embodiment of a conventional saccharification and fermentation method.

Claims (1)

【特許請求の範囲】[Claims] 原料を糖化発酵するに当り、原料を最初のタンクに受け
入れてから、その後に並列に配置した複数個のタンクに
移動させ、それぞれのタンクで一定時間滞留させてから
糖化醪を得ることを特徴とする糖化発酵方法。
When saccharifying and fermenting raw materials, the raw materials are received in the first tank, then transferred to multiple tanks arranged in parallel, and left in each tank for a certain period of time to obtain saccharified moromi. A saccharification and fermentation method.
JP1338732A 1989-12-28 1989-12-28 Fermentation with saccharification Pending JPH03201973A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1338732A JPH03201973A (en) 1989-12-28 1989-12-28 Fermentation with saccharification

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1338732A JPH03201973A (en) 1989-12-28 1989-12-28 Fermentation with saccharification

Publications (1)

Publication Number Publication Date
JPH03201973A true JPH03201973A (en) 1991-09-03

Family

ID=18320941

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1338732A Pending JPH03201973A (en) 1989-12-28 1989-12-28 Fermentation with saccharification

Country Status (1)

Country Link
JP (1) JPH03201973A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112852622A (en) * 2021-02-06 2021-05-28 江苏信息职业技术学院 Saccharification equipment and saccharification method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112852622A (en) * 2021-02-06 2021-05-28 江苏信息职业技术学院 Saccharification equipment and saccharification method
CN112852622B (en) * 2021-02-06 2023-08-29 江苏信息职业技术学院 Saccharification equipment and saccharification method

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