JPS59159774A - Selection of grown seed of yeast - Google Patents

Selection of grown seed of yeast

Info

Publication number
JPS59159774A
JPS59159774A JP3541583A JP3541583A JPS59159774A JP S59159774 A JPS59159774 A JP S59159774A JP 3541583 A JP3541583 A JP 3541583A JP 3541583 A JP3541583 A JP 3541583A JP S59159774 A JPS59159774 A JP S59159774A
Authority
JP
Japan
Prior art keywords
yeast
solution
conditions
dispersion
floating
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
JP3541583A
Other languages
Japanese (ja)
Inventor
Takashi Komata
小俣 隆司
Shinji Yamada
真司 山田
Katatsune Murata
村田 容常
Kozo Kamata
鎌田 耕造
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.)
Sapporo Breweries Ltd
Original Assignee
Sapporo Breweries 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 Sapporo Breweries Ltd filed Critical Sapporo Breweries Ltd
Priority to JP3541583A priority Critical patent/JPS59159774A/en
Publication of JPS59159774A publication Critical patent/JPS59159774A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain grown seed of yeast having given cohesiveness and dispersibility without carrying out fermentation test, by screening a yeast rapidly precipitating under agglomeration conditions and floating longer under dispersion conditions. CONSTITUTION:A yeast is suspended in a solution having pH and saccharide concentration adjusted to values suitable for agglomeration and dispersion, namely, a solution having fermentation period to carry out agglomeration and dispersion of yeast, or a solution made into the same conditions, the suspension is allowed to stand for a given time, the precipitated or floating yeast is collected, this yeast is suspended in a solution having pH and saccharide concentration adjusted to values suitable for agglomeration and dispersion, the suspension is allowed to stand for a given time, and the floating or precipitated yeast is collected.

Description

【発明の詳細な説明】 本発明は酵母の育種選抜法に関し、詳しくは所望の凝集
性と分散性を有する酵母の育種選抜法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for breeding and selecting yeast, and more particularly to a method for breeding and selecting yeast having desired flocculation and dispersibility.

酵母はビール、清酒、ワインなどの酒類の製造をはじめ
として様々な分野で利用されている。ところが、たとえ
ばビール醸造においては何らかの原因で酵母の沈降性が
次第に変化してくる場合がある。このような現象は発酵
管理の上で好ましくないことである。また、発酵条件1
作業条件の変更等によって凝集性の異なる酵母が要求さ
れることがある。
Yeast is used in a variety of fields, including the production of alcoholic beverages such as beer, sake, and wine. However, for example, in beer brewing, the settling ability of yeast may gradually change for some reason. Such a phenomenon is undesirable in terms of fermentation management. In addition, fermentation conditions 1
Yeast with different flocculating properties may be required due to changes in working conditions, etc.

酵母の凝集・分散性を自由にコントロールすることを目
的として、特定の性質をもった酵母を選抜する方法が知
られている。しかし、これらの従来法は発酵試験を実施
して確認する必要があるため、長時間を要するばかシで
なく、客観的な判定が困難であったシ、試験条件により
結果が変動し信頼性が低い等の多くの問題点がある。
A method of selecting yeast with specific properties is known for the purpose of freely controlling the flocculation and dispersibility of yeast. However, these conventional methods require confirmation by conducting fermentation tests, which are not only time-consuming, but also difficult to objectively judge, and the results vary depending on the test conditions, making them unreliable. There are many problems such as low

本発明者らは、酵母の凝集・分散は細胞表面の物理化学
性が周囲の条件によって変化するために生起する現象で
あると考えており、発酵試験を行なわなくても凝集条件
で速やかに沈降し、分散条件でよシ長く浮遊する酵母を
スクリーニングして行けば、適度の凝集・分散性をもつ
酵母が育種選抜できると考え、検討を重ねた。その結果
、本発明を完成するに到ったのである。
The present inventors believe that yeast flocculation and dispersion are phenomena that occur because the physicochemical properties of the cell surface change depending on the surrounding conditions, and that yeast sedimentation occurs quickly under flocculation conditions even without a fermentation test. However, we thought that if we screened for yeast that could float for a long time under dispersion conditions, we would be able to breed and select yeast with appropriate flocculation and dispersibility, and we conducted repeated studies. As a result, the present invention was completed.

本発明は、下記の工程を含む酵母の育種選抜法である。The present invention is a yeast breeding and selection method including the following steps.

(イ)酵母を凝集もしくは分散させたいpHおよび糖濃
度に調節された溶液に酵母を懸濁させる工程、 (ロ)所定時間静置後、沈でんした酵母もしくは浮遊し
ている酵母を回収する工程、 (ハ)酵母を分散もしくは凝集させたいpHおよび糖濃
度に調節された溶液に懸濁させる工程、に)所定時間静
置後、浮遊している酵母もしくは沈でんした酵母を回収
する工程、 本発明における工程(イ)もしくは(ハ)の凝集条件に
用いる溶液は、具体的には酵母の凝集を実現させたい発
酵時期の液体ないしはそれと同等の条件とした溶液を意
味する。たとえば、ビール醸造にあっては、発酵を完了
したときのビール組成のものを用いる。すなわち、酵母
を凝集させたい時の条件を備えた溶液である。この場合
、pHと糖濃度を調節することが重要であるが、ほかに
酵母の凝集に関与する物質(たとえば大麦、麦芽ないし
は麦汁中に存在する酵母凝集性の有機物および無機塩類
など)を含有させることも必要である。なお、ビールの
ようにガスを含む場合は、気泡などによって酵母が浮上
してしまうため、正確な検定が困難となる。し、fcが
′つて、このような場合はガス抜きした溶液を用いるべ
きである。ガス抜きビールのほか果汁、穀物糖化液を発
酵させたもの、さらには後記する非発酵性オリゴ糖やそ
の誘導体などを使用することができる。ビール酵母を対
象とする場合は、pHA 8〜4.8.糖濃度5%以下
、通常は0.1〜3%程度に調節した溶液が好ましい。
(b) A step of suspending yeast in a solution adjusted to the desired pH and sugar concentration for flocculating or dispersing yeast; (b) A step of collecting settled yeast or floating yeast after standing for a predetermined period of time; (c) a step of suspending yeast in a solution adjusted to the desired pH and sugar concentration for dispersion or flocculation, and (c) a step of recovering floating or settled yeast after standing for a predetermined period of time. Specifically, the solution used for the flocculation conditions in step (a) or (c) refers to a liquid at the fermentation period in which yeast flocculation is desired to be achieved, or a solution under conditions equivalent thereto. For example, in beer brewing, the beer composition used when fermentation is completed. In other words, it is a solution that has the conditions required to flocculate yeast. In this case, it is important to adjust the pH and sugar concentration, but also contain substances that are involved in yeast flocculation (e.g., yeast flocculating organic substances and inorganic salts present in barley, malt, or wort). It is also necessary to Note that when beer contains gas, yeast floats to the surface due to air bubbles, making accurate assay difficult. However, in such a case, a degassed solution should be used. In addition to degassed beer, fruit juice, fermented grain saccharified liquid, and non-fermentable oligosaccharides and their derivatives, which will be described later, can be used. When targeting brewer's yeast, pHA is 8 to 4.8. Preferably, the solution has a sugar concentration of 5% or less, usually about 0.1 to 3%.

これは酵母が凝集を実現することを期待される条件であ
る。したがって、発酵を限界まで進行させたい場合は0
%に近くシ、発酵後残糖を5%にすることを期待する場
合には5%を選ぶことになる。酵母を懸濁させる場合、
酵母濃度がα001〜α5fi’/IIL/、好ましく
はα01〜α1 p/m7となるようにすべぎである。
This is the condition under which yeast would be expected to achieve flocculation. Therefore, if you want fermentation to proceed to the limit, 0
If you expect the residual sugar to be 5% after fermentation, choose 5%. When suspending yeast,
The yeast concentration should be α001 to α5fi'/IIL/, preferably α01 to α1 p/m7.

また、溶液を収答する容器としては縦長の、たとえばビ
ューレット型ガラス管などが望ましい。
Further, as a container for storing the solution, a vertically long container such as a buret-type glass tube is preferable.

次に、工程(ロ)における静置条件については特に制限
はrLいが、低温で静置することが望ましく、通常は0
〜60°C1好ましぐは0〜20°Cの温度にて1分〜
48時間、好ましくは2〜24時間静置する。所定時間
の静置後、沈でんした酵母もしくは浮遊している酵母を
回収する。酵母の回収は適当な手段により行なえばよく
、たとえばビューレット型ガラス管を用いたと、きは、
沈でんした酵母を該容器の底部から静かに抜取ればよい
。また、浮遊している酵母の回収は懸濁液を集めて遠心
分離、濾過などによシ行なえばよい。
Next, there are no particular restrictions on the standing conditions in step (b), but it is desirable to stand at a low temperature, usually 0.
〜60℃1 Preferably 1 minute at a temperature of 0 to 20℃〜
Let stand for 48 hours, preferably 2 to 24 hours. After standing still for a predetermined period of time, settled yeast or floating yeast is collected. Yeast may be recovered by any appropriate means, such as using a burette-type glass tube,
The settled yeast may be gently removed from the bottom of the container. Further, floating yeast can be collected by collecting the suspension and performing centrifugation, filtration, etc.

工程(ハ)もしくは(イ)において分散条件に用いる溶
液は、前記凝集条件の場合とは反対に酵母の分散を実現
させたい発酵時期の液体ないしはそれと同等の条件とし
た溶液を意味する。この場合も、溶液のpHと糖濃度を
適切に調節することが必要である。分散条件は発酵を促
進させ家い時の条件である。このときは主に非発酵性の
糖類を含む溶液が用いられ、具体的には非発酵性オリゴ
糖やその誘導体などがあり、たとえばヘキソースまたは
その誘導体(たとえばソルボース、マンノース、D−グ
ルコサミン、α−メチル−D−グルコシド、α−メチル
−D−ガラクトシドなど)、セロビオース、サリシン、
アルブチン、トレハロース、ラクトース、ソルビトール
、マンニトールなトカある。
The solution used for the dispersion conditions in step (c) or (a) refers to the liquid at the fermentation stage where yeast dispersion is desired to be achieved, as opposed to the aggregation conditions described above, or a solution under conditions equivalent thereto. In this case as well, it is necessary to appropriately adjust the pH and sugar concentration of the solution. Dispersion conditions are conditions that promote fermentation. At this time, a solution containing mainly non-fermentable sugars is used, specifically non-fermentable oligosaccharides and their derivatives, such as hexoses or their derivatives (such as sorbose, mannose, D-glucosamine, α- methyl-D-glucoside, α-methyl-D-galactoside, etc.), cellobiose, salicin,
These include arbutin, trehalose, lactose, sorbitol, and mannitol.

溶液中の非発酵性糖類の濃度は目的とする酵母の分散性
または凝集性のレベルを考慮して決められ、通常は2〜
50%、好ましくは4〜20%の範囲内で選定する。ま
た、非発酵性糖類の溶媒としては水のほか各種水溶液を
使用できるが、通常は緩衝液、たとえばQ、1M酢酸緩
衝液(TIH5,0〜60)などを用いる。ここで用い
る8器としては前記と同じビューレット型ガラス容器が
好ましい。また、静置は低温で行なうことが好ましく、
通常は0〜60°d1好ましくは0〜20℃とする。
The concentration of non-fermentable saccharides in the solution is determined by considering the level of dispersibility or flocculation of the target yeast, and is usually between 2 and 3.
50%, preferably within the range of 4 to 20%. Furthermore, as a solvent for non-fermentable saccharides, various aqueous solutions other than water can be used, but buffers such as Q, 1M acetate buffer (TIH 5,0-60), etc. are usually used. As the eight vessels used here, the same burette type glass container as mentioned above is preferable. In addition, it is preferable to leave it at a low temperature.
The temperature is usually 0 to 60°d1, preferably 0 to 20°C.

次罠、工程に)における静置条件、特に時間については
格別の制限はなく、1分以上7日間程度、通常は50分
〜24時間静置したのち、浮遊している酵母もしくは沈
でんした酵母を回収する。静置時間は容器の形状、静置
温度などを考慮して決定する。酵母の回収は、沈でんし
たものを除いた懸濁液を集め、遠心分離、濾過などの操
作により行なうことができる。また、沈でんした酵母の
回収は@器の底部から静かに抜取ることなどにより行な
えばよい。
There are no particular restrictions on the standing conditions (especially the time) in (next trap, step), and after leaving it standing for 1 minute or more for about 7 days, usually 50 minutes to 24 hours, the floating yeast or settled yeast is removed. to recover. The standing time is determined by considering the shape of the container, the standing temperature, etc. Yeast can be recovered by collecting the suspension excluding precipitated matter and performing operations such as centrifugation and filtration. Further, the settled yeast may be recovered by gently pulling it out from the bottom of the container.

なお、別法として上記工程(ハ)における非発酵性オリ
ゴ糖の代りK発酵性の糖類を含有した溶液帆とえば麦汁
など)を使用することができる。この場合は酵母を懸濁
してから長時間静置すると発酵が行なわれ、酵母が浮き
上がるため正確な検定が不可能となるので、静置時間は
0℃で1分〜24時間、好ましくは1〜5時間程度の短
時間とすべきである。さらには、このような発酵性溶液
を用いる場合は、酵母が発酵を行なわない条件(ただし
、好ましくは酵母の活性を低下させない範囲内)、たと
えば低温、加圧2発酵阻害剤の添加などの条件下に行な
う必要がある。具体的には一2〜0°Cという低温で1
2時間以内、0〜10°Cでα5〜skg/c++!の
加圧下24〜48時間、あるいは抗生物質(アクチジオ
ンなど)やモノヨード酢酸(α005〜0.01%程度
)等の発酵阻害剤を加える方法があり、これらを単独で
もしくは適宜組合せることができる。なお、塩類の添加
は凝集性に影響を与えるため好ましくない。
Alternatively, instead of the non-fermentable oligosaccharides in step (c) above, a solution containing fermentable sugars (such as wort) can be used. In this case, if the yeast is suspended and left for a long time, fermentation will occur and the yeast will float, making accurate assay impossible. It should be a short period of time, about 5 hours. Furthermore, when using such a fermentable solution, conditions such as conditions that do not allow yeast to ferment (but preferably within a range that does not reduce the activity of yeast), such as low temperature, pressure, addition of a fermentation inhibitor, etc. It needs to be done below. Specifically, at a low temperature of -2 to 0°C,
α5~skg/c++ at 0~10°C within 2 hours! For 24 to 48 hours under pressure, or by adding a fermentation inhibitor such as an antibiotic (such as actidione) or monoiodoacetic acid (α005 to about 0.01%), and these methods can be used alone or in combination as appropriate. Note that addition of salts is not preferable because it affects cohesiveness.

上記工程(イ)γに)はその順序は任意であり、また工
程(ハ)およびに)については複数回、通常は4〜6回
繰返すことが好ましい。
The above steps (a) and γ) can be carried out in any order, and it is preferable to repeat steps (c) and 2) multiple times, usually 4 to 6 times.

以上の如く、本発明によれば凝集させたい時期に凝集・
沈降し、分散させたい時期に分散・浮遊する酵母を選抜
することができる。本発明の方法は適宜に条件を変更す
ることによりビール酵母のほか清酒酵母、ワイン酵母、
ウィスキー酵母。
As described above, according to the present invention, agglomeration and
It is possible to select yeast that will settle and disperse and float at the desired time of dispersion. By appropriately changing the conditions, the method of the present invention can be applied to brewer's yeast, sake yeast, wine yeast, etc.
whiskey yeast.

アルコール酵母などの様々な酵母に適用することができ
る。
It can be applied to various yeasts such as alcoholic yeast.

次に、本発明を実施例によシ説明する。Next, the present invention will be explained using examples.

実施例1 麦汁で静置培養したビール酵母(サツカロミセス・ウバ
ルム エAM 4206)  2 tをガス抜キヒール
(pH4,1,糖度1.8%)2(1m/に懸濁し、2
0m容のビューレットに入れ静置した。2時間後、容器
底部よシ沈でんしている酵母を抜取った。
Example 1 2 t of brewer's yeast (Saccharomyces ubarum AE AM 4206), which had been statically cultured in wort, was suspended in 2 (1 m/ml) of degassed Kiheel (pH 4.1, sugar content 1.8%),
It was placed in a 0 m capacity burette and left standing. After 2 hours, the yeast that had settled to the bottom of the container was removed.

次に、この抜取シ酵母の全量を5%のα−メチル−D−
グルコシド01M酢酸級衝液(pH5,5)201に懸
濁し、2Qml容のビューレットに入れ静置した。1昼
夜放置した後、沈でんした酵母を除いた酵母懸濁液を集
め、遠心分離を行なって酵母を回収した。
Next, the entire amount of this sampled yeast was mixed with 5% α-methyl-D-
The suspension was suspended in 201 glucoside 01M acetic acid-grade buffer solution (pH 5.5), placed in a 2Qml buret, and left to stand. After standing for a day and night, the yeast suspension from which the settled yeast had been removed was collected and centrifuged to recover the yeast.

しかる後、5%のα−メチル−D−グルコシド溶液(p
H5−5)に酵母を懸濁、静置、遠沈による酵母の回収
という操作を4回繰返した。
Thereafter, a 5% α-methyl-D-glucoside solution (p
The operations of suspending yeast in H5-5), standing still, and recovering yeast by centrifugation were repeated four times.

このようにして得た酵母を麦汁寒天培地で25’C,4
8時間平板培養した。この培養物から大きいコロニー4
株を釣菌し、それぞれを麦汁で20’C,48時間培養
し7辷。得られた酵母について凝集試験を行なった。す
f’iわち、各酵母0.61を酢酸緩唾液(PH4,2
)  1’Oifに懸濁して血沈管にとり、60分後の
沈降酵母の扁さを比較した。
The yeast thus obtained was placed on a wort agar medium at 25'C, 4
Plated for 8 hours. From this culture 4 large colonies
The strains were harvested and each strain was cultured in wort at 20'C for 48 hours until 7 days old. A flocculation test was conducted on the obtained yeast. That is, 0.61 of each yeast was mixed with acetic acid (pH 4.2).
) The yeast was suspended in 1'Oif and taken into a blood sedimentation tube, and the flatness of the sedimented yeast was compared after 60 minutes.

次に、4株中最大の凝集沈降性を示した1株を再び麦汁
で20℃、48時間培養した。この培養で得た酵母につ
いて前記した凝集・分散選抜法を2回繰返したのち、再
び麦汁寒天培地で25℃。
Next, the one strain that showed the greatest flocculation-sedimentation property among the four strains was cultured again in wort at 20° C. for 48 hours. After repeating the flocculation/dispersion selection method described above twice for the yeast obtained by this culture, the yeast was cultured again on a wort agar medium at 25°C.

48時間平板培養した。この培養物から10株を釣菌し
、それぞれを再び麦汁寒天培地で平板培養した。得られ
た酵母について上記と同様にして凝集試験を行なった。
Plated for 48 hours. Ten strains were picked from this culture, and each strain was cultured again on a wort agar medium. The obtained yeast was subjected to an agglutination test in the same manner as above.

なお、この場合、対照として親株を同一条件で試験して
比較した。結果を第1図に示す。
In this case, as a control, the parent strain was tested under the same conditions for comparison. The results are shown in Figure 1.

図から明らかなとおシ、選抜した10株はいずれも親株
よシも凝集性が強いものであった。この酵母はpH4,
2、糖濃度0%で凝集し、pH5,5、糖濃度5%で分
散する性質を有している。
As is clear from the figure, all of the 10 selected strains had strong aggregation properties, both as well as the parent strain. This yeast has a pH of 4,
2. It has the property of aggregating at a sugar concentration of 0% and dispersing at a pH of 5.5 and a sugar concentration of 5%.

実施例2 実施例1のガス抜きビールの代シにガス抜きダイエツト
ビール(pH4,8、エキス(13%)を用い、かつ5
1%のα−メチル−p−グルコシド溶液の代シに4%の
ラクトース溶液を用いたこと以外は実施例1と同様に行
なってダイエツトビール用酵母を選抜した。この酵母は
pH4,3、糖濃度11.3%で凝集し、pH6,0、
糖濃度5%で分散する性質をしている。
Example 2 Degassed diet beer (pH 4.8, extract (13%) was used as a substitute for the degassed beer of Example 1, and
Yeast for diet beer was selected in the same manner as in Example 1, except that a 4% lactose solution was used instead of the 1% α-methyl-p-glucoside solution. This yeast aggregates at pH 4.3 and sugar concentration 11.3%, and at pH 6.0,
It has the property of dispersing at a sugar concentration of 5%.

実施例3 実施例1において、最初に分散条件を設定し次いで凝集
条件を設定したこと以外は同様にし処理したところ、実
IFi例1と同様の分散性・凝性を有する酵母が得られ
た。
Example 3 When the yeast was treated in the same manner as in Example 1 except that the dispersion conditions were first set and then the flocculation conditions were set, yeast having the same dispersibility and flocculation properties as in Actual IFi Example 1 was obtained.

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

第1図は本発明の方法によシ選抜した酵母にいて行なっ
た凝集試験の結果を示すグラフであ特許出願人 サッポ
ロビール株式会社 代理 人 弁理士 久保田藤部 fJ来
FIG. 1 is a graph showing the results of an agglutination test conducted on yeast selected by the method of the present invention. Patent applicant: Sapporo Breweries Ltd., patent attorney: Kubota Fujibe f.J.

Claims (1)

【特許請求の範囲】 1、 下記の工程を含む酵母の育種選抜法。 (イ)酵母を凝集もしくは分散させたいpHおよび糖濃
度に調節された溶液に酵母を懸濁させる工程、 (ロ)所定時間静置後、沈でんした酵母もしくは浮遊し
ている酵母を回収する工程、 (ハ)酵母を分散もしくは凝集させたいpHおよび糖濃
度に調節された溶液に懸濁させる工程、に)所定時間静
置後、浮遊している酵母もしくは沈でんした酵母を回収
する工程、
[Claims] 1. A yeast breeding and selection method comprising the following steps. (b) A step of suspending yeast in a solution adjusted to the desired pH and sugar concentration for flocculating or dispersing yeast; (b) A step of collecting settled yeast or floating yeast after standing for a predetermined period of time; (c) a step of suspending yeast in a solution adjusted to the desired pH and sugar concentration for dispersion or flocculation, and (c) a step of collecting floating or settled yeast after standing for a predetermined period of time.
JP3541583A 1983-03-04 1983-03-04 Selection of grown seed of yeast Pending JPS59159774A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3541583A JPS59159774A (en) 1983-03-04 1983-03-04 Selection of grown seed of yeast

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3541583A JPS59159774A (en) 1983-03-04 1983-03-04 Selection of grown seed of yeast

Publications (1)

Publication Number Publication Date
JPS59159774A true JPS59159774A (en) 1984-09-10

Family

ID=12441241

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3541583A Pending JPS59159774A (en) 1983-03-04 1983-03-04 Selection of grown seed of yeast

Country Status (1)

Country Link
JP (1) JPS59159774A (en)

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