JPS6366190B2 - - Google Patents

Info

Publication number
JPS6366190B2
JPS6366190B2 JP61076021A JP7602186A JPS6366190B2 JP S6366190 B2 JPS6366190 B2 JP S6366190B2 JP 61076021 A JP61076021 A JP 61076021A JP 7602186 A JP7602186 A JP 7602186A JP S6366190 B2 JPS6366190 B2 JP S6366190B2
Authority
JP
Japan
Prior art keywords
yeast
immobilized
column
continuous fermentation
tank
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
JP61076021A
Other languages
Japanese (ja)
Other versions
JPS62232374A (en
Inventor
Masato Hirotsune
Fujio Nakada
Masaaki Hamachi
Takemitsu Pponma
Yataro Nunokawa
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.)
KH Neochem Co Ltd
Original Assignee
Kyowa Hakko Kogyo 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 Kyowa Hakko Kogyo Co Ltd filed Critical Kyowa Hakko Kogyo Co Ltd
Priority to JP61076021A priority Critical patent/JPS62232374A/en
Publication of JPS62232374A publication Critical patent/JPS62232374A/en
Publication of JPS6366190B2 publication Critical patent/JPS6366190B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Alcoholic Beverages (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は、固定化酵母により酒類を連続醗酵す
る技術に関するもので、前槽を設け、原料糖液の
雑菌汚染を防ぎながら長期間安定して、すぐれた
品質の酒類を生産する製造法に関する。 [従来の技術] 固定化酵母によるアルコールの連続生産は、す
でに実用化の段階にある。酒類の連続生産に関し
てもワインやビールの連続醸造が試みられてい
る。これら酒類の連続醸造においては、雑菌汚染
対策および最終の製品の品質が、特に問題となつ
ている。 従来の連続醗酵における雑菌(特に細菌)汚染
対策としては、原料糖液の煮沸殺菌(ビール等)
あるいは、原料糖液に、酸を添加してPHを4.0以
下にする(アルコール、ワイン)方法が用いられ
ている。しかし、煮沸殺菌した原料糖液を連続し
て長期間、無菌的に通液する事は、現場的には、
かなり困難であり、コストも高くなる。また原料
糖液のPHを下げた場合においては、蒸留を行わな
い酒類では、製品の酸度も高くなり、酸味の強い
ものになる。さらに、いずれの方法においても連
続醗酵カラムに送るまでの糖液の保存が問題とな
る。特に固形の澱粉質原料を用いる酒類の場合、
バツチ式で糖化を行い、糖化液とした後にカラム
へ連続的に通液する方式となるため、糖液の保存
は、大きな問題である。 [発明が解決しようとする問題点] 本発明が解決しようとする問題点は、上記従来
技術の難点を解消し、すべての酒類に応用可能な
連続醗酵生産法を提供する事である。すなわち、
原料糖液の煮沸殺菌やPH調整を行わなくても、糖
液の保存が可能であり、且つ雑菌汚染のない連続
醸造を長期間行う方法を提供するものである。 [問題点を解決するための手段] 上記問題点は、連続醗酵に用いる固定化酵母カ
ラムの前に遊離酵母を含ませた前槽を設け、生成
したアルコールの存在下で、必要な酵母を数多く
保つた状態にしておき、その前槽に糖液を添加す
る事により達成される。さらに、この前槽に続く
固定化酵母カラム内は、前槽を設けない従来の方
式の状態に比べてアルコール濃度と、酵母数を高
く保てるために、雑菌汚染はなくなり最終的に生
成する酒類のアルコール濃度も高くなる。 本発明は、基本的には、固定化酵母カラムの前
に、遊離酵母も含んだ前槽を設けて、酒類の連続
醗酵を行う製造法であり、前槽内では、底部に沈
澱する酵母を、撹拌する事により浮遊状態に保つ
方法を含有される。本発明において、前槽に含ま
せる遊離酵母は、別途培養したものを、添加して
もよいが、連続醗酵をスタートする前の段階にお
いて、固定化酵母カラムと前槽とを循環させて固
定化増殖酵母より溶出してくる遊離酵母を、前槽
内で増殖させる方法が、より有効である。前槽内
において、酵母が増殖すると、アルコールが生成
されるが、そのアルコール濃度を4%以上に保つ
事により前槽内、ひいては固定化酵母カラム内の
細菌による汚染を防ぐことができる。 本発明に使用する酵母は、アルコール醗酵や醸
造に通常用いられる酵母ならば、いずれでもよい
が、野性酵母に対してキラー活性を有しているキ
ラー酵母を用いる方法も含有される。 [発明の効果] 本発明の連続醗酵法によれば、固形の原料を、
バツチ式で糖化した糖化液を、煮沸殺菌やPHを
4.0以下に調整することなく、長期間にわたり雑
菌汚染のない連続生産が可能となるため、現場ス
ケールにおいても、低コストで安定した酒類が製
造できる。さらに、清酒のように酸味の少ない酒
類の場合でも酸度の低い製品を連続醸造すること
が可能である。さらに本発明により、連続醸造し
た酒類の成分は、従来のバツチ式で製造した製品
と比較して差は認められず、官能においては、む
しろ優れているものである。 [実施例] 次に、実施例を挙げて本発明をさらに詳しく説
明するが、これらに限定されるものではない。 実施例 1 常法に従い、米粉を酵素剤で液化、糖化した
後、炭素濾過したものと、米麹を糖化し、炭素濾
過した麹糖化液とを混合し、直糖を20%に、PHは
約5.5のものを乳酸を用いてPH4.0にそれぞれ調整
して、連続醗酵用の糖化液とした。第1図参照。 常法に従い、育種したキラー協会10号酵母を、
公知の方法により、アルギン酸ナトリウムで固定
化し、得られたキラー10号固定化酵母ゲル100ml
を300mlのカラムに充填した。前槽に糖化液600ml
を入れ、固定化酵母カラムと接続して糖化液を循
環させた。前槽の温度は15℃、固定化酵母のカラ
ムは20℃とした。4日間循環させて、アルコール
濃度が4%を超えた時点より固定化酵母カラムよ
り溶出してくる醗酵液を別の溶器に採取し、連続
醗酵を開始した。流速は、10ml/hr(SV0.1)で
一定とした。前槽には、翌日より毎日減少した分
だけの糖化液(240ml)を追加した。前槽のアル
コール濃度を1〜5%(平均3%)に保つた場合
においては、細菌による汚染があり、酸度も上昇
したが、前槽のアルコール濃度を3〜7%(平均
5%)または4〜8%(平均6%)に保つた場合
は、運転日数が長期にわたる場合でも、細菌によ
る汚染もなく、酸度も一定していた。さらに、野
性酵母による汚染も認められなかつた。この条件
で固定化酵母カラムより溶出してきた連続醗酵液
のアルコール濃度は10日目以降、12〜13%(v/
v)と高い値であり、1ケ月以上安定していた。
第2a図〜第2d図参照。 実施例 2 実施例1と同様に調整した米粉糖化液のPHを、
4.0、4.5、5.5(未調整)と変えた3種類の糖化液
を用意した。 実施例1と同様に調整した固定化酵母カラムと
撹拌装置付きの前槽を接続したリアクター3台を
用意し、それぞれの前槽にPHの異なる3種類の糖
化液400mlを加えた。実施例1と同様の方法で、
前槽のアルコール濃度をすべて4〜8%(平均6
%)に保つた。前槽の温度15℃、固定化酵母カラ
ム20℃、流速10ml/hr(SV0.1)の条件で、11〜
12%のアルコールが、1.5月以上安定して生成さ
れた。酸度の生成は、いずれの場合においても一
定であり、上昇は見られなかつた。第3a図〜第
3d図参照。 連続醗酵中の溶出液を調べたところ、前槽の撹
拌を行つた場合においては、PH4.0、4.5、5.5のい
ずれの糖化液を用いてもバクテアや野性酵母は検
出されなかつた。第1表参照。 連続醗酵溶出液を5℃で1週間貯蔵後、遠心分
離により酵母を除いて分析および利酒を行つた。
バツチ式で製造したコントロールに比べて、成分
的に、差は認められなかつた。官能検査では、PH
5.5(PH未調整)の糖化液を用いて、前槽の撹拌を
行つた区分がもつとも優れていた。第2表参照。
[Industrial Application Field] The present invention relates to a technology for continuous fermentation of alcoholic beverages using immobilized yeast, which is provided with a pre-tank, and is capable of producing alcoholic beverages of excellent quality stably for a long period of time while preventing bacterial contamination of the raw sugar solution. Concerning the manufacturing method for producing. [Prior Art] Continuous production of alcohol using immobilized yeast is already at the stage of practical application. Regarding the continuous production of alcoholic beverages, attempts have been made to continuously brew wine and beer. In the continuous brewing of these alcoholic beverages, countermeasures against bacterial contamination and quality of the final product are particularly problematic. As a countermeasure against contamination by various bacteria (especially bacteria) during conventional continuous fermentation, boiling sterilization of the raw sugar solution (beer, etc.)
Alternatively, a method is used in which acid is added to the raw sugar solution to lower the pH to below 4.0 (alcohol, wine). However, in the field, it is difficult to continuously pass boiling-sterilized raw sugar solution aseptically for a long period of time.
This is quite difficult and costly. Furthermore, when the pH of the raw sugar solution is lowered, the acidity of the alcoholic beverage that is not distilled increases, resulting in a product with a strong sour taste. Furthermore, in either method, storage of the sugar solution before sending it to the continuous fermentation column poses a problem. Especially in the case of alcoholic beverages that use solid starchy raw materials,
Since saccharification is performed in batches and the saccharified solution is continuously passed through the column, storage of the saccharide solution is a major problem. [Problems to be Solved by the Invention] The problems to be solved by the present invention are to solve the problems of the above-mentioned conventional techniques and to provide a continuous fermentation production method that can be applied to all alcoholic beverages. That is,
To provide a method in which sugar solution can be stored without boiling sterilization or pH adjustment of the raw material sugar solution, and continuous brewing can be carried out for a long period of time without bacterial contamination. [Means for solving the problem] The above problem can be solved by installing a pre-tank containing free yeast in front of the immobilized yeast column used for continuous fermentation, and collecting a large number of necessary yeast in the presence of the generated alcohol. This is achieved by keeping it in a maintained state and adding sugar solution to the pre-tank. Furthermore, in the immobilized yeast column following this pre-tank, the alcohol concentration and number of yeast can be kept higher than in the conventional system without a pre-tank, so there is no bacterial contamination and the final alcoholic beverage is Alcohol concentration also increases. The present invention is basically a manufacturing method in which a pre-tank containing free yeast is provided in front of an immobilized yeast column, and continuous fermentation of alcoholic beverages is carried out. , contains a method of keeping it in a suspended state by stirring. In the present invention, the free yeast contained in the pre-tank may be cultured separately and added, but the immobilized yeast may be immobilized by circulating the immobilized yeast column and the pre-tank before starting continuous fermentation. More effective is a method in which free yeast eluted from propagating yeast is grown in a pre-tank. When yeast grows in the front tank, alcohol is produced, but by keeping the alcohol concentration at 4% or more, it is possible to prevent bacterial contamination in the front tank and, by extension, in the immobilized yeast column. The yeast used in the present invention may be any yeast commonly used in alcohol fermentation or brewing, but it also includes a method using killer yeast that has killer activity against wild yeast. [Effect of the invention] According to the continuous fermentation method of the present invention, solid raw materials can be
The saccharified liquid that has been saccharified in batches is sterilized by boiling and the pH is
Since continuous production without bacterial contamination is possible for a long period of time without adjusting the temperature below 4.0, stable alcoholic beverages can be produced at low cost even on an on-site scale. Furthermore, even in the case of alcoholic beverages with low acidity, such as sake, it is possible to continuously brew products with low acidity. Further, according to the present invention, there is no discernible difference in the components of the continuously brewed alcoholic beverages compared to products produced by the conventional batch method, and the alcoholic beverages are rather superior in terms of sensory experience. [Example] Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited thereto. Example 1 According to a conventional method, rice flour was liquefied and saccharified using an enzyme agent, and then carbon-filtered, and a koji saccharification liquid obtained by saccharifying rice malt and carbon-filtering was mixed. The pH of approximately 5.5 was adjusted to 4.0 using lactic acid, and a saccharification solution for continuous fermentation was prepared. See Figure 1. Killer Association No. 10 yeast, bred according to conventional methods,
100ml of Killer No. 10 immobilized yeast gel obtained by immobilization with sodium alginate by a known method
was packed into a 300ml column. 600ml of saccharification liquid in the front tank
was connected to the immobilized yeast column and the saccharification solution was circulated. The temperature of the pre-tank was 15°C, and the temperature of the immobilized yeast column was 20°C. After 4 days of circulation, the fermentation solution eluted from the immobilized yeast column was collected into another vessel when the alcohol concentration exceeded 4%, and continuous fermentation was started. The flow rate was kept constant at 10 ml/hr (SV0.1). The amount of saccharification solution (240 ml) that decreased each day from the next day was added to the front tank. When the alcohol concentration in the front tank was maintained at 1 to 5% (average 3%), there was bacterial contamination and the acidity increased; When maintained at 4 to 8% (average 6%), there was no bacterial contamination and the acidity remained constant even after long operating days. Furthermore, no contamination with wild yeast was observed. Under these conditions, the alcohol concentration of the continuous fermentation solution eluted from the immobilized yeast column was 12-13% (v/
v), which was a high value and remained stable for more than a month.
See Figures 2a to 2d. Example 2 The pH of the rice flour saccharification solution adjusted in the same manner as in Example 1 was
Three types of saccharification solutions were prepared: 4.0, 4.5, and 5.5 (unadjusted). Three reactors were prepared in which an immobilized yeast column prepared in the same manner as in Example 1 was connected to a front tank equipped with a stirring device, and 400 ml of three types of saccharification solutions with different pHs were added to each front tank. In the same manner as in Example 1,
The alcohol concentration in the front tank is all 4-8% (average 6%).
%). Under the conditions of pre-tank temperature 15℃, immobilized yeast column 20℃, flow rate 10ml/hr (SV0.1),
12% alcohol was produced stably over 1.5 months. The production of acidity was constant in all cases and no increase was observed. See Figures 3a to 3d. When the eluate during continuous fermentation was examined, no bactea or wild yeast was detected when the pre-tank was stirred, regardless of whether the saccharification solution at pH 4.0, 4.5, or 5.5 was used. See Table 1. After storing the continuous fermentation eluate at 5° C. for one week, yeast was removed by centrifugation and analysis and alcohol consumption were performed.
No difference was observed in terms of composition compared to the batch-produced control. In the sensory test, PH
The classification using a saccharification solution of 5.5 (PH not adjusted) and stirring in the front tank was also excellent in terms of durability. See Table 2.

【表】【table】

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

第1図は、実施例1における米粉糖化液の調製
法を示すフローチヤート、第2a図は、実施例1
における連続醗酵装置図、第2b図〜第2d図は
連続醗酵液の性状を示すグラフ、第3a図は、実
施例2における連続醗酵装置図、第3b図〜第3
d図は連続醗酵液の性状を示すグラフである。
Figure 1 is a flowchart showing the method for preparing the saccharified rice flour solution in Example 1, and Figure 2a is a flowchart showing the method for preparing the saccharified rice flour solution in Example 1.
Figures 2b to 2d are graphs showing the properties of the continuous fermentation liquid, Figure 3a is a diagram of the continuous fermentation apparatus in Example 2, and Figures 3b to 3.
Figure d is a graph showing the properties of the continuous fermentation solution.

Claims (1)

【特許請求の範囲】 1 固定化酵母を用いる連続醗酵法により酒類を
生産する際、固定化酵母カラムの前に、遊離酵母
を含んだ前槽を設けることを特徴とする、固定化
酵母による酒類の連続醗酵法。 2 遊離酵母を含んだ前槽を撹拌する事により、
前槽内の酵母を浮遊状態に保つ特許請求の範囲第
1項記載の方法。 3 前槽に含ませる酵母は、固定化酵母カラムよ
り溶出してくる遊離の酵母を還流して利用する、
特許請求の範囲第1項記載の方法。 4 遊離酵母を含む前槽のアルコール濃度が4%
以上である特許請求の範囲第1項記載の方法。 5 用いる糖液が未殺菌である特許請求の範囲第
1項記載の方法。 6 固定化に使用する酵母がキラー酵母である特
許請求の範囲第1項記載の方法。
[Scope of Claims] 1. Alcoholic beverages produced by immobilized yeast, characterized in that when producing alcoholic beverages by a continuous fermentation method using immobilized yeast, a front tank containing free yeast is provided in front of the immobilized yeast column. continuous fermentation method. 2. By stirring the pretank containing free yeast,
The method according to claim 1, wherein the yeast in the front tank is kept in a suspended state. 3. The yeast contained in the front tank is used by refluxing free yeast eluted from the immobilized yeast column.
A method according to claim 1. 4 Alcohol concentration in the front tank containing free yeast is 4%
The method according to claim 1, which is the above. 5. The method according to claim 1, wherein the sugar solution used is unsterilized. 6. The method according to claim 1, wherein the yeast used for immobilization is killer yeast.
JP61076021A 1986-04-01 1986-04-01 Continuous fermentation of liquor using immobilized yeast Granted JPS62232374A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61076021A JPS62232374A (en) 1986-04-01 1986-04-01 Continuous fermentation of liquor using immobilized yeast

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61076021A JPS62232374A (en) 1986-04-01 1986-04-01 Continuous fermentation of liquor using immobilized yeast

Publications (2)

Publication Number Publication Date
JPS62232374A JPS62232374A (en) 1987-10-12
JPS6366190B2 true JPS6366190B2 (en) 1988-12-20

Family

ID=13593171

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61076021A Granted JPS62232374A (en) 1986-04-01 1986-04-01 Continuous fermentation of liquor using immobilized yeast

Country Status (1)

Country Link
JP (1) JPS62232374A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03164188A (en) * 1988-09-30 1991-07-16 Sanou Techno Insuteichiyuuto Kk Production of ethanol with free cell and immobilized cell using agglutinative yeast

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0673445B2 (en) * 1984-08-31 1994-09-21 麒麟麦酒株式会社 Liquor manufacturing method

Also Published As

Publication number Publication date
JPS62232374A (en) 1987-10-12

Similar Documents

Publication Publication Date Title
Bhat et al. An overview on the biological production of vinegar
EP0361165B1 (en) Method using immobilized yeast to produce ethanol and alcoholic beverages
US4380552A (en) Method of deacidifying wine and composition therefor
CN101220331A (en) A kind of preparation method of double-bacteria fermented red raspberry whole juice fruit wine
US4915959A (en) Method for the continuous maturation of fermented beer
EP1263925A2 (en) Method of aerating yeast prior to pitching
EP0900838B1 (en) Citrus fruit vinegar and method for producing the same
JPS6366190B2 (en)
JPH06319514A (en) Beverage clarification method
JP2007166975A (en) Black vinegar production method and black vinegar produced by the method
CN1055114C (en) Method for producing yangtao juice beer
CN109666575A (en) Hickory chick health-care vinegar and morel beverage vinegar
US3402048A (en) Process for producing beer of the vollbier type
JP2004298109A (en) Method for producing alcoholic beverage and alcoholic beverage
US20090238919A1 (en) Method of manufacturing vinegar with high extract content
JP3968183B2 (en) Production method of malt alcoholic beverage
JPH10276755A (en) Production of sake
JP2654632B2 (en) Sake brewing method
CN120924363A (en) Preparation method of mulberry yellow wine
JP3725295B2 (en) Liquor production method and liquor
JP3586819B2 (en) Alcohol production method
JPS61195681A (en) Preparation of antiseptic japanese sake
JPS63304974A (en) Method for brewing sparklng sake in short period
RU2304611C2 (en) Method for producing beer, method for treatment of brewing yeast and yeast suspension composition for brewing
CN120737920A (en) Brewing method of yellow rice wine