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JPS5841833B2 - How to treat liquid medium after fermentation - Google Patents
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JPS5841833B2 - How to treat liquid medium after fermentation - Google Patents

How to treat liquid medium after fermentation

Info

Publication number
JPS5841833B2
JPS5841833B2 JP52027602A JP2760277A JPS5841833B2 JP S5841833 B2 JPS5841833 B2 JP S5841833B2 JP 52027602 A JP52027602 A JP 52027602A JP 2760277 A JP2760277 A JP 2760277A JP S5841833 B2 JPS5841833 B2 JP S5841833B2
Authority
JP
Japan
Prior art keywords
yeast
fermentation
liquid medium
liquid
beer
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
JP52027602A
Other languages
Japanese (ja)
Other versions
JPS53113077A (en
Inventor
冨治 中谷
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.)
Kirin Brewery Co Ltd
Original Assignee
Kirin Brewery Co 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 Kirin Brewery Co Ltd filed Critical Kirin Brewery Co Ltd
Priority to JP52027602A priority Critical patent/JPS5841833B2/en
Publication of JPS53113077A publication Critical patent/JPS53113077A/en
Publication of JPS5841833B2 publication Critical patent/JPS5841833B2/en
Expired legal-status Critical Current

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Description

【発明の詳細な説明】 〔I〕発明の背景 本発明は、醗酵を終了した液体培地から微生物を分離回
収する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [I] Background of the Invention The present invention relates to a method for separating and recovering microorganisms from a liquid medium that has undergone fermentation.

別の観点からみれば、本発明は、醗酵を終了した液体培
地から液体醗酵生成物を分離回収する方法に関する。
Viewed from another perspective, the present invention relates to a method for separating and recovering a liquid fermentation product from a liquid medium that has undergone fermentation.

さらに具体的には、本発明はたとえばビールの醸造の際
の残渣酵母から濃縮酵母を回収する方法に関する。
More specifically, the present invention relates to a method for recovering concentrated yeast from residual yeast, for example during the brewing of beer.

我が国においてビール製造に使用される酵母(下面醗酵
ビール酵母)は、主醗酵や後醗酵が終りに近づくと、醗
酵槽の底部に沈殿して半製品ビールと分れる。
Yeast used in beer production in Japan (bottom-fermenting beer yeast) settles at the bottom of the fermentation tank and separates into semi-finished beer when the main fermentation and post-fermentation are nearing completion.

このようにして分離した酵母すなわち残渣酵母はかなり
の量(たとえば、醗酵槽中の全半製品の約2V/V%)
に達する。
The yeast thus separated, i.e. residual yeast, is present in a considerable amount (e.g. approximately 2 V/V% of the total semi-finished product in the fermenter).
reach.

醗酵液からデカンテーション等によって分離された残渣
酵母は固形分含量15〜20重量%程度のものであり、
80〜85重量%程度の半製品ビールが含まれている。
The residual yeast separated from the fermentation liquid by decantation etc. has a solid content of about 15 to 20% by weight,
Contains about 80-85% by weight of semi-finished beer.

従来はこの残渣酵母は酵母の回収ということで利用され
ていただけであって、含まれている半製品ビールは分離
回収されることなく廃棄されていた。
In the past, this residual yeast was only used to recover the yeast, and the semi-finished beer contained therein was discarded without being separated and recovered.

すなわち、酵母濃度が高い残渣酵母を大気圧下で静置し
ておくと、大部分の酵母は沈殿するが一部は残存糖分が
醗酵して発生する炭酸ガスによりスカム状に液面に浮上
して厚い層をなし、酵母−半製品ビール−酵母の三層に
分れ、半製品ビールのみ効率よく回収することがむづか
しいので、酵母と一緒に洗浄して、回収酵母を得ている
In other words, if residual yeast with a high concentration of yeast is left to stand under atmospheric pressure, most of the yeast will settle, but some will rise to the surface of the liquid in the form of a scum due to the carbon dioxide gas generated by fermentation of the residual sugar. It forms a thick layer and is divided into three layers: yeast, semi-finished beer, and yeast, and it is difficult to efficiently recover only the semi-finished beer, so it is washed together with the yeast to obtain the recovered yeast.

その場合、上記中間層のビールは回収されずに廃棄され
ており、また回収されるのは最下層の酵母であって上層
Q酵母は回収困難なため廃棄されているので、工程の歩
留りが悪くなっていると共に排水のCOD負荷が著るし
く大きくなるため多額の設備投資や運転費が必要となっ
ていたのである。
In that case, the beer in the middle layer is discarded without being recovered, and the yeast in the bottom layer is recovered, and the Q yeast in the upper layer is discarded because it is difficult to recover, so the yield of the process is poor. At the same time, the COD load of wastewater becomes significantly large, requiring large amounts of capital investment and operating costs.

このような観点から、また最近の醸造技術の進歩にも支
えられて、いままで廃棄されていた残渣酵母中の半製品
ビールおよび酵母を回収することカ海外でも検討されて
いる。
From this point of view, and with the support of recent advances in brewing technology, recovery of semi-finished beer and yeast from residual yeast that has been discarded is being considered overseas as well.

しかし、これらはいずれもr過機や遠心分離機を用いて
酵母とビールを分離回収するものであるので多額の設備
投資と多大の労力および動力を要するという問題があり
、省力化の進んだ工場では労力の負担が相対的に大きく
なるため実用化は困難である。
However, these methods all use filtration machines and centrifuges to separate and recover yeast and beer, so they require a large amount of capital investment, labor, and power. However, it is difficult to put it into practical use because the labor burden is relatively large.

このような問題は単にビール製造の場合だけでなく、醗
酵を終了した液体培地から微生物と液体醗酵生成物とを
分離回収しようとする場合に一般に認められることであ
る。
Such problems occur not only in beer production, but also in general when trying to separate and recover microorganisms and liquid fermentation products from a liquid medium after fermentation.

(1)発明の概要 本発明は上記の点に解決を与えることを目的とし、醗酵
終了後の液体培地を加圧下に静置することによってこの
目的を達成しようとするものである。
(1) Summary of the Invention The present invention aims to provide a solution to the above-mentioned problems, and attempts to achieve this purpose by allowing the liquid medium after fermentation to stand still under pressure.

従って、本発明による醗酵終了後の液体培地の処理法は
、固体成分と液体成分を含む醗酵終了後の液体培地を、
該液体成分の一部を除去してから、加圧下に静置して固
体成分の沈降を促進すること、を特徴とするものである
Therefore, the method for treating a liquid medium after fermentation according to the present invention is to treat a liquid medium containing a solid component and a liquid component after fermentation.
The method is characterized in that after a part of the liquid component is removed, it is allowed to stand still under pressure to promote sedimentation of the solid component.

このように、本発明は、従来開放容器ないし非加圧密閉
容器中で行なわれていた醗酵終了液体培地の液体成分(
以下、ビールで代表させる)と固体成分(以下、酵母で
代表させる)の沈降分離を加圧下に行なうことによって
、従来生じていた酵母の一部の浮上を伴なうことなくそ
の事実上全量を沈降させてビールおよび酵母の回収率を
向上させることに成功したものである。
As described above, the present invention provides a solution to the liquid component (
By performing sedimentation separation of solid components (hereinafter referred to as beer) and solid components (hereinafter referred to as yeast) under pressure, virtually the entire amount of yeast can be removed without the levitation of a part of the yeast that conventionally occurs. We succeeded in improving the recovery rate of beer and yeast by sedimentation.

本発明では加圧といってもビール、酵母の状況にもよる
が、たとえば0.5 kg/crtt (ゲージ)程度
以上の圧力があれば十分であるから、従来の密閉容器を
そのまNあるいは多少耐圧性にするだけで使用すること
ができ、また加圧手段としては代表的には空気その他の
気体の圧入によるから、設備投資の増加は僅かなもので
あると共に省力化が可能である。
In the present invention, pressurization depends on the conditions of the beer and yeast, but for example, a pressure of about 0.5 kg/crtt (gauge) or higher is sufficient, so a conventional closed container can be used as it is with N or It can be used simply by making it somewhat pressure resistant, and since the pressurizing means is typically the injection of air or other gas, the increase in equipment investment is small and labor can be saved.

また、液体成分の一部を除去することも、通常は液体成
分中に含まれる醗酵産物を回収するために当然に行なわ
れることでもある。
Additionally, removing a portion of the liquid component is also normally carried out in order to recover the fermentation products contained in the liquid component.

従って、たとえば、酵母を分離用沈降槽に入れである時
間(たとえば−昼夜)加圧下に静置し、沈降した酵母を
印加されている圧力によって槽外に排出させるだけで、
回収可能ビールの50〜60%程度(全残渣酵母の40
〜50%程度)がほとんど無人で回収できる。
Therefore, for example, by simply placing yeast in a separation sedimentation tank, leaving it under pressure for a certain period of time (for example, day and night), and expelling the settled yeast out of the tank by the applied pressure,
Approximately 50-60% of the recoverable beer (40% of the total residual yeast)
~50%) can be collected almost unattended.

しかも、酵母は従来と同様に再利用が可能である。Furthermore, yeast can be reused in the same way as before.

また、従来は酵母の回収および洗浄作業が醗酵終了後の
一時期に集中して設備および作業面での困難さを生んで
いたが、本発明方法によれば酵母処理作業の時間的制約
が大きく緩和されることになる。
In addition, in the past, yeast recovery and cleaning work was concentrated for a period of time after the completion of fermentation, creating difficulties in terms of equipment and work, but with the method of the present invention, time constraints on yeast processing work are greatly alleviated. will be done.

0発明の詳細な説明 1、醗酵終了後の液体培地 固体成分と液体成分とを含む醗酵終了後の液体培地が一
般に本発明の対象となる。
0 Detailed Description of the Invention 1. Liquid medium after fermentation A liquid medium after fermentation comprising a solid component and a liquid component is generally the subject of the present invention.

具体的には、たとえば、ビール醗酵液、日本酒醗酵液等
がある。
Specifically, there are, for example, beer fermentation liquid, Japanese sake fermentation liquid, and the like.

そして、本発明で対象とする液体培地は、この液体培地
から該液体成分の一部を除去したものであって、具体的
にはたとえば沈降分離された固体成分濃縮物(たとえば
ビール醸造の際の残渣酵母)である。
The liquid medium targeted by the present invention is obtained by removing a part of the liquid components from this liquid medium, and specifically, for example, a solid component concentrate that has been sedimented and separated (for example, during beer brewing) residual yeast).

醗酵終了後の醗酵液の一つの代表例は、ビール醗酵液で
ある。
One representative example of the fermented liquor after completion of fermentation is beer fermented liquor.

そして、さらに具体的には、醗酵槽、特に主醗酵槽、か
ら回収された残渣酵母である。
And, more specifically, it is the residual yeast recovered from the fermenter, especially the main fermenter.

これは、主醗酵□液からデカンテーション等によって回
収され、固形分15〜20重量%程度のものである。
This is recovered from the main fermentation liquid by decantation or the like, and has a solid content of about 15 to 20% by weight.

以下の説明においては、この主醗酵終了後の残渣酵母に
ついて本発明を説明する。
In the following explanation, the present invention will be explained with respect to the residual yeast after the completion of the main fermentation.

2、加圧 加圧は、シリンダ内でのピストンによる加圧のような剛
性面による加圧の外に、密閉タンク内への気体の圧入に
よっても行なうことができる。
2. Pressurization Pressurization can be performed not only by pressurization by a rigid surface such as pressurization by a piston in a cylinder, but also by pressurizing gas into a closed tank.

最も好ましいのは、気体の圧入による加圧である。The most preferable method is pressurization by injecting gas.

加圧用の気体は、回収すべき半製品ビールないし酵母に
対して悪影響を与えないものならば任意である。
Any pressurizing gas may be used as long as it does not have an adverse effect on the semi-finished beer or yeast to be recovered.

経済的見地からは空気および二酸化炭素が適当である。From an economic point of view, air and carbon dioxide are suitable.

主醗酵終了後、醗酵槽から回収された残渣酵母を密閉式
沈降槽に集め、槽内に空気を圧入し、好ましくは槽内圧
力を一定に保ちつつ静置する。
After completion of the main fermentation, residual yeast recovered from the fermentation tank is collected in a closed sedimentation tank, air is forced into the tank, and the tank is preferably allowed to stand still while keeping the internal pressure constant.

加圧しない場合に認められる酵母の浮上およびスカム形
成が抑制されて、酵母は自然に沈降を続ける。
The flotation and scum formation of yeast observed when no pressure is applied is suppressed, and the yeast continues to settle naturally.

その結果、酵母は沈降槽底部に沈澱して、槽上部にはビ
ール槽ができる。
As a result, the yeast settles to the bottom of the settling tank, and a beer tank forms at the top of the tank.

槽底部の排出口をあければ、槽内圧力によって沈澱酵母
は排出される。
If the outlet at the bottom of the tank is opened, the precipitated yeast will be discharged by the pressure inside the tank.

固液の分離は経時的に進行するが、その効果は対数曲線
的に現われる。
Solid-liquid separation progresses over time, and its effect appears in a logarithmic curve.

3−沈降槽を使用し、1.8kg/ca(ゲージ)空気
圧下に静置した場合の主醗酵終了残渣酵母の固液分離効
果の一例は、下表に示す通りである。
3-An example of the solid-liquid separation effect of the main fermentation residue yeast when a sedimentation tank is used and left under an air pressure of 1.8 kg/ca (gauge) is as shown in the table below.

国体分離効果は、酵母の生理状態を如何に管理するかに
よって異なるもののようである。
The effect of national isolation seems to vary depending on how the physiological state of the yeast is managed.

また、下記のような工程管理上の諸要素によっても左右
される。
It also depends on various process control factors such as the following.

(1)品温 品温が適当に高い方が分離効果がよい。(1) Product temperature The separation effect is better when the product temperature is appropriately high.

特に、静時間が短いときにそうである(固液分離効果は
、品温によって左右される)。
This is especially true when the settling time is short (the solid-liquid separation effect depends on the product temperature).

具体的には、たとえば0〜20℃、好ましくは3〜8℃
程度であることがふつうである。
Specifically, for example, 0 to 20°C, preferably 3 to 8°C
It is normal that it is about a certain degree.

50J沈降槽を使用し、1.8 kg/crA (ゲー
ジ)空気圧下に静置した場合の固液分離効果の一例な品
温5℃および15℃の場合について示せば、下表に示す
通りである。
An example of the solid-liquid separation effect when using a 50J sedimentation tank and standing under an air pressure of 1.8 kg/crA (gauge) at product temperatures of 5°C and 15°C is as shown in the table below. be.

(2)圧力 圧力は、設備、作業、安全等の面から低い方が望ましく
、酵母生理上からも低いことが望ましいが、あまり低い
とスカム状に酵母層が浮上することが多い。
(2) Pressure It is desirable that the pressure be low from the standpoint of equipment, work, safety, etc., and also from the viewpoint of yeast physiology, but if the pressure is too low, the yeast layer often floats in the form of a scum.

具体的な圧力は他の条件(たとえば品温)を考慮して簡
単な実験によって知ることができるが、たとえば品温が
5℃程度の場合には0、5〜1.5 kg/crA (
ゲージ)で十分な効果が得られる。
The specific pressure can be determined by a simple experiment taking into account other conditions (for example, product temperature), but for example, if the product temperature is around 5°C, the
Gauge) can provide sufficient effect.

(3)沈降槽容積および酵母量 沈降槽容積や槽内酵母量によっても分離の状況は異なる
もののようである。
(3) Sedimentation Tank Volume and Yeast Amount The separation situation seems to vary depending on the sedimentation tank volume and the amount of yeast in the tank.

一般に、小規模の場合は、現場規模程度の場合に比べて
分離速度および分離効果が悪い。
Generally, in a small-scale case, the separation speed and separation effect are lower than in a field-scale case.

Claims (1)

【特許請求の範囲】[Claims] 1 固体成分と液体成分とを含む醗酵終了後の液体培地
を該液体成分の一部を除去してから、加圧下に静置して
固体成分の沈降を促進させることを特徴とする、醗酵終
了後の液体培地の処理法。
1. Termination of fermentation, which is characterized by removing part of the liquid medium from a liquid medium containing solid components and liquid components after completion of fermentation, and then leaving the medium under pressure to promote sedimentation of the solid components. How to process the liquid medium afterwards.
JP52027602A 1977-03-15 1977-03-15 How to treat liquid medium after fermentation Expired JPS5841833B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52027602A JPS5841833B2 (en) 1977-03-15 1977-03-15 How to treat liquid medium after fermentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52027602A JPS5841833B2 (en) 1977-03-15 1977-03-15 How to treat liquid medium after fermentation

Publications (2)

Publication Number Publication Date
JPS53113077A JPS53113077A (en) 1978-10-03
JPS5841833B2 true JPS5841833B2 (en) 1983-09-14

Family

ID=12225462

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52027602A Expired JPS5841833B2 (en) 1977-03-15 1977-03-15 How to treat liquid medium after fermentation

Country Status (1)

Country Link
JP (1) JPS5841833B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62273358A (en) * 1986-05-22 1987-11-27 寺島 憲治 Ceiling, wall and floor structure of building
JPS62276158A (en) * 1986-05-22 1987-12-01 寺島 憲治 Ceiling, wall and floor structure of building
JPH01129338U (en) * 1988-02-16 1989-09-04

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6005784B1 (en) * 2015-03-24 2016-10-12 油長酒造株式会社 Liquor top tank method
CN107849504A (en) * 2015-05-14 2018-03-27 南非大学 Waste beer reclaims

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
BRANWISSEUSCHAFT=1974 *
BRAUWELT=1954 *
BRAUWISSEUSCHAFT=1974 *
EUROPEAU BREWERY CONVENTION PROCEECLIUG OF 15TH CONGRESS=1975 *
MODER BREWING TECHNOLOGY=1971 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62273358A (en) * 1986-05-22 1987-11-27 寺島 憲治 Ceiling, wall and floor structure of building
JPS62276158A (en) * 1986-05-22 1987-12-01 寺島 憲治 Ceiling, wall and floor structure of building
JPH01129338U (en) * 1988-02-16 1989-09-04

Also Published As

Publication number Publication date
JPS53113077A (en) 1978-10-03

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