JPH0685709B2 - Method for producing sake with low alcohol concentration - Google Patents

Method for producing sake with low alcohol concentration

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Publication number
JPH0685709B2
JPH0685709B2 JP13168685A JP13168685A JPH0685709B2 JP H0685709 B2 JPH0685709 B2 JP H0685709B2 JP 13168685 A JP13168685 A JP 13168685A JP 13168685 A JP13168685 A JP 13168685A JP H0685709 B2 JPH0685709 B2 JP H0685709B2
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JP
Japan
Prior art keywords
sake
fermentation
saccharification
alcohol concentration
taste
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 - Lifetime
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JP13168685A
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Japanese (ja)
Other versions
JPS61289875A (en
Inventor
孝 徳山
健 岸本
嘉久 松尾
奈加子 田嶋
Original Assignee
株式会社創研
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Priority to JP13168685A priority Critical patent/JPH0685709B2/en
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Publication of JPH0685709B2 publication Critical patent/JPH0685709B2/en
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Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、加熱失活によつて糖化と発酵を分離し、低ア
ルコール濃度の任意の時点で発酵を止めることにより、
嫌味、イグ味を出すことなく、簡単に、しかも甘辛の調
節も自由にでき、さらには酸添加によつて、清酒の風味
も自由に変えることのできる多様な低アルコール濃度清
酒の製造法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention separates saccharification and fermentation by heat inactivation, and stops fermentation at any time of low alcohol concentration,
The present invention relates to a variety of low alcohol concentration sake production methods that can easily and freely adjust sweetness and spiciness without giving off tastes and harshness, and can also change the flavor of sake by adding acid. Is.

(従来の技術) 近年、清酒の需要が落ち込み、業界をあげて需要要喚起
に躍起となつている。この需要低下の理由の一つとし
て、実際に飲まれる段階での清酒のアルコール濃度の高
さ(16%前後)が指摘されている。例えば、ウイスキー
のアルコール濃度は高いが、ほとんど水割で飲まれ、一
般に、このときのアルコール濃度は10%前後といわれて
いる。ところが、一般の清酒は、アルコール濃度が14〜
15%をきると、味の調和がくずれ、水つぼくなり飲用に
供し難くなる。
(Prior Art) In recent years, the demand for sake has fallen, and the industry as a whole is rushing to call for demand. It has been pointed out that one of the reasons for this decrease in demand is the high alcohol concentration of sake (around 16%) when it is actually drunk. For example, whiskey has a high alcohol concentration, but most of it is drunk with water, and it is generally said that the alcohol concentration at this time is around 10%. However, general sake has an alcohol concentration of 14-
When it falls below 15%, the harmony of taste is lost, and it becomes hard to drink because it becomes watery.

そこで、低アルコール濃度清酒については、清酒の需要
拡大のため多くの研究開発がなされているが、これらは
基本的には、純米醸造のごとき濃醇酒をつくり、これを
割水する方法、あるいは普通の仕込みをして、醪の後半
に追い水をしていく方法がとられている。しかし、これ
らの方法では低アルコール濃度といつても12%前後が限
界である。また、低アルコール濃度清酒といつても味の
面では、従来の清酒と同様の風味をもつている。中には
ブドウ酒酵母、焼酎用麹菌等を使つて型を変えたものも
見られるが、これとても品質には大きな差は認められな
い。
Therefore, for low alcohol concentration sake, many researches and developments have been made to expand the demand for sake, but basically, these are methods of making concentrated sake such as pure rice brewing and watering it. The usual method is to prepare and then add water in the latter half of the mash. However, these methods are limited to low alcohol concentrations and around 12% at all times. In addition, it has a flavor similar to that of conventional sake, in terms of taste always with low alcohol concentration sake. Some of them have been changed in shape using wine yeast, shochu, or koji mold for shochu, but there is no significant difference in quality.

そこで、本発明者は、多酸存在下で糖化発酵を行なうこ
とによる低アルコール濃度清酒の製造法を発明した。こ
れは、糖とアルコールのバランスがとれた、しかも、従
来の清酒とは全く異なる優れた風味をもつものである。
しかし、この方法によるものは、酸度が高く、糖含量も
高いもので、糖と酸の関係をみると、ハニーワイン、ポ
ートワインといつた種類に属するものである。すなわ
ち、これは甘口タイプであり、辛口タイプにしようとす
ると、どうしても渋味、イグ味が出てしまうものであ
る。
Therefore, the present inventor has invented a method for producing low alcohol concentration sake by performing saccharification and fermentation in the presence of polyacid. This has a good balance of sugar and alcohol, and has an excellent flavor completely different from conventional sake.
However, this method has a high acidity and a high sugar content, and when looking at the relationship between sugar and acid, it belongs to honey wine and port wine. That is, this is a sweet type, and when the dry type is used, the astringent taste and the squid taste are inevitably produced.

本発明者は、さらに、発酵の途中で上槽し、酵母または
酒母を添加して糖化発酵または発酵のみを行い、風味エ
キス分を調整する方法を発明した。しかし、この方法
は、2度発酵を行うための手間がかかること、その上、
甘辛の調整範囲が狭いという欠点がある。
The present inventor has further invented a method of adjusting a flavor extract content by adding a yeast or liquor to a saccharification fermentation or fermentation only in a tank in the middle of fermentation. However, this method requires time and labor for performing the fermentation twice, and moreover,
There is a drawback that the adjustment range of sweet and spicy is narrow.

(発明が解決しようとする問題点) 前述のように、従来の製造法では、嫌味、イグ味がな
く、甘辛の調整が自由にでき、しかも、風味までも自由
に調整できる低アルコール濃度清酒は未だに存在しな
い。
(Problems to be Solved by the Invention) As described above, according to the conventional production method, there is no disagreeable taste, no harsh taste, and sweetness and spiciness can be freely adjusted. It doesn't exist yet.

(問題を解決する手段) 本発明者らは、永年の研究の結果、加熱失活により糖化
と発酵を分離し、低アルコール濃度の任意の時点で発酵
を止めることで、嫌味やイグ味がなく、甘口、辛口を自
由に調整することができることを見い出した。また、発
酵開始時に多酸存在下におくと、清酒風味が全くなくな
り、酸添加なしで発酵させると、清酒風味が出現するこ
とを見い出し、本発明を完成するに至つたのである。
(Means for Solving the Problem) As a result of many years of research, the present inventors separated saccharification and fermentation by heat inactivation, and stopped fermentation at an arbitrary point of low alcohol concentration, so that there was no harshness or astringency. It was found that the sweetness and dryness can be adjusted freely. Further, it was found that when the fermentation was started in the presence of polyacid, the flavor of sake was completely lost, and when fermentation was carried out without the addition of acid, the flavor of sake appeared, and the present invention was completed.

本発明でいう低アルコール濃度とは、アルコール濃度が
13%以下のものを示し、多酸存在下とは、酸度が発酵開
始時および途中、終了後のいかなる時点においても3.5
以上を指す。
The low alcohol concentration in the present invention means that the alcohol concentration is
In the presence of polyacid, the acidity is 3.5% at the start of fermentation, on the way, and at any time after completion.
Refers to the above.

次に製造方法の詳細について説明する。Next, details of the manufacturing method will be described.

まず、常法により、蒸米、米麹を製造する。ついで、こ
れらに加水し、高温で糖化させる。加水は最終の甘辛調
整および目的の味つけによつて、くみ水歩合100〜200%
あるいはそれ以上または以下でもよい。高温糖化は一般
に50〜65℃の間で行うが、糖化さえすればよいため、こ
の範囲外でも可能である。このようにして生成した糖化
液をそのまま、あるいは搾汁後、加熱して酵素を失活さ
せ、糖化を完了させる。一般に、温度は65〜100℃の間
で行い、時間は温度に応じて決めればよい。なお、糖化
酵素を完全に失活させる必要はなく、65℃以下でもよい
が、より高温で完全に失活した方がイグ味が少なく、糖
化と発酵を完全に分離することが、より好ましいといえ
る。また、糖化後、上槽はしてもしなくても品質には影
響はみられない。しかし、上槽し搾汁した方が、後の製
造が簡単であり、製品が安定している。
First, steamed rice and rice koji are produced by a conventional method. Then, they are hydrated and saccharified at high temperature. The water content is 100-200% for the water ratio depending on the final adjustment of sweetness and seasoning.
Alternatively, it may be higher or lower. High-temperature saccharification is generally carried out at 50 to 65 ° C, but since saccharification is sufficient, it is possible to use it outside this range. The saccharified liquid thus produced is heated as it is or after being squeezed to inactivate the enzyme to complete the saccharification. Generally, the temperature is between 65 and 100 ° C., and the time may be determined according to the temperature. Incidentally, it is not necessary to completely inactivate the saccharifying enzyme, but it may be 65 ° C or lower, but it is more preferable to completely inactivate the saccharifying enzyme at a higher temperature, and it is more preferable to completely separate saccharification and fermentation. I can say. In addition, after saccharification, the quality is not affected with or without the upper tank. However, the later production is easier and the product is more stable when the upper tank is squeezed.

次に、この加熱液を冷却し、酵母を添加して発酵を行
う。使用酵母は、7号、9号、ワイン等のいずれでもよ
い。この発酵の段階は、初め20〜25℃で増殖を行つても
よいし、初めから低温発酵を行つてもよい。また、加熱
時に殺菌がなされているため、酸添加は必ずしも必要で
はない。しかし、多酸存在下では、全く新しいタイプの
清酒、すなわち、清酒風味のない清酒ができることが、
後述の官能検査の結果よりわかつた。このようにして発
酵を行い、目的とするアルコール度数、エキス分量等に
達したところで上槽し、火入れする。
Next, this heated liquid is cooled and yeast is added to perform fermentation. The yeast used may be No. 7, No. 9 or wine. In this fermentation step, growth may be initially carried out at 20 to 25 ° C, or low temperature fermentation may be carried out from the beginning. In addition, acid addition is not always necessary because it is sterilized during heating. However, in the presence of polyacid, a completely new type of sake, that is, sake with no sake flavor, can be produced.
It was found from the result of the sensory test described below. Fermentation is carried out in this manner, and when the desired alcohol content, extract content, etc. are reached, the fermentation is carried out in the upper tank and fired.

上記の工程を経て得られる本製品においては、甘口領域
では全く渋味がみられず、また、さらに発酵を行い、辛
口を得るときも嫌味、イグ味が全くない。甘辛の調整
は、発酵によつてばかりでなく、麹歩合、糖化の行い
方、くみ水歩合の調整によつてもでき、実際には、これ
らの組合わせによつて行う。
In the product obtained through the above steps, no astringency is observed in the sweet region, and even when fermentation is performed to obtain dryness, there is no dislike or irritation. The sweetness and spiciness can be adjusted not only by fermentation, but also by adjusting the koji rate, the saccharification method, and the kumimizu rate, and in practice, the combination thereof is used.

なお、加熱失活を行わない場合、糖化と発酵を同時に行
つても、また、高温糖化後、発酵を行つても、あるいは
高温糖化後、圧搾過をし、液発酵を行つても、辛口
領域で嫌味、イグ味が発生し、一般的な並行復発酵とい
う従来の製造方法では、本発明製品のような優れた品質
のものはできない。
In addition, when heat inactivation is not carried out, even if saccharification and fermentation are carried out at the same time, or even after high-temperature saccharification and fermentation, or after high-temperature saccharification, squeezing and liquid fermentation are carried out, it is a dry area. However, the conventional production method of general parallel re-fermentation cannot produce a product of excellent quality like the product of the present invention.

(発明の効果) 本来、清酒の製造工程の特徴は、糖化と発酵を同時に行
う並行復発酵である。しかし、以上述べたように、清酒
の製造工程の糖化と発酵を、加熱失活によつて分離する
という簡単な方法によつて、嫌味、イグ味がなく、甘
辛、風味も自由に調節できる低アルコール濃度清酒が得
られる。嫌味、イグ味があると飲み飽きしてしまうこと
が、後述の官能検査より明らかであり、現実の商品とし
ては、その価値はなく、イグ味のないものということ
は、飲料の基本である。このイグ味の除去は、製造工程
における技術の熟練等の差異には関係なく、加熱失活と
いう工程を加えることにより得られる効果である。
(Effect of the Invention) Originally, the characteristic feature of the manufacturing process of sake is the parallel re-fermentation in which saccharification and fermentation are simultaneously performed. However, as mentioned above, by the simple method of separating saccharification and fermentation in the production process of sake by heat deactivation, there is no harshness, no irritation, and sweetness and flavor can be freely controlled. Alcohol concentration Sake is obtained. It is clear from the sensory test described below that the user will get tired of drinking if he / she has a bad taste or a bad taste, and it is the basic value of a drink that it is not worth it as an actual product and that it does not have a bad taste. This removal of the squid taste is an effect obtained by adding a step of heat deactivation regardless of differences in technical skill in the manufacturing process.

さらに、従来の低アルコール濃度清酒は、濃醇酒を割水
したり、醪の後半に追い水をしたり、糖化液発酵をし
たり等のいずれも並行復発酵であり、これらの製品は、
その方法の特徴により実質的に決まる単一的味、風味、
甘辛となつてしまう。しかし、本発明は、加熱失活によ
つて糖化と発酵を分離し、低アルコール濃度の任意の時
点で発酵を止めることにより、上述のように嫌味、イグ
味を出すことがないだけでなく、甘辛の調節をはじめ、
種々の味の調整が簡単にできる。また、酸添加によつて
清酒風味も自由に変えることができる。
Furthermore, conventional low alcohol concentration sake is parallel re-fermentation, such as watering concentrated sake, replenishing water in the second half of the mash, saccharified liquid fermentation, etc., and these products are
A single taste, flavor that is substantially determined by the characteristics of the method,
It will be sweet and spicy. However, the present invention, by separating the saccharification and fermentation by heat inactivation, by stopping the fermentation at any time of low alcohol concentration, as described above, not only do not give off taste, ig taste, Start adjusting sweet and spicy,
Easy adjustment of various tastes. In addition, the flavor of sake can be freely changed by adding acid.

したがつて、消費者の要求に幅広く答えられるように、
品質、設計も自由にできるという画期的製造方法であ
り、各種のタイプの低アルコール濃度清酒を得ることが
可能となる。
Therefore, to meet a wide range of consumer demands,
This is an epoch-making manufacturing method in which the quality and design can be freely set, and various types of low alcohol concentration sake can be obtained.

本発明に関して行つた官能検査であるが、まず、イグ味
に関する官能検査の結果について、表1および2に示し
た。
Regarding the sensory test conducted for the present invention, first, the results of the sensory test for the immature taste are shown in Tables 1 and 2.

この表1,2に示されたように、本発明による製品では、
イグ味があると答えた人は一人もいないが、加熱失活に
よる糖化と発酵の分離を行わなかつた場合、特に辛口の
ものに対しては、全員がイグ味があると答え、飲み飽き
してくると答えた。この結果より、糖化後、加熱失活を
行うことは、イグ味の除去という効果が顕著に表われて
いるといえる。
As shown in Tables 1 and 2, in the product according to the present invention,
None of the respondents answered that they had an igu taste, but when they did not separate saccharification and fermentation by heat deactivation, all responded that they had an igu taste, especially those that were dry, and tired of drinking them. I will come. From these results, it can be said that the effect of heat deactivation after saccharification has a remarkable effect of removing the astringency.

しかも、酵母の種類に関係なく、また、温度経過にも関
係なく、常温で放置していてもイグ味の発生はみられ
ず、製造方法も発酵の打ち切り時点に関係なく、イグ味
の発生がみられなかつたことは、本製造方法の非常に大
きな特徴である。すなわち、誰でもが簡単に、かつ品質
設計(消費者の多様な品質要求に答えられる)低アルコ
ール濃度清酒が自由にできることは、画期的な製造方法
であるといえる。
Moreover, regardless of the type of yeast, and regardless of the temperature progress, even if left at room temperature, the occurrence of igu taste is not seen, and the production method does not occur regardless of the fermentation termination time What has not been seen is a very significant feature of this manufacturing method. In other words, it is an epoch-making manufacturing method that anyone can easily make quality designs (satisfying various quality demands of consumers) of low alcohol concentration sake.

さらに、清酒風味について官能検査を行い、その結果を
表3および4に示した。
Furthermore, a sensory test was performed on the sake flavor, and the results are shown in Tables 3 and 4.

このように酸添加を行つたものについては、全員が清酒
風味はないとし、酸添加していないものは、全員が清酒
風味があると答えた。この結果より、本発明製造法は、
清酒風味の嫌いな人も飲むことができ、アルコール飲料
に弱い人でも気軽に飲めるという低アルコール濃度清酒
ができることを示している。
As for those to which acid was added in this way, all said that there was no flavor of sake, and those to which acid was not added all answered that they had flavor of sake. From this result, the production method of the present invention is
It shows that people who do not like the sake flavor can drink sake, and even people who are weak in alcoholic drinks can easily drink sake with a low alcohol concentration.

以上のように、本発明は、糖化後、加熱によつて、ある
程度以上の酵素の失活を行い、糖化と発酵を分離させる
ことによつて、飲み飽きの原因となるイグ味のない製品
を簡単に製造することができる。さらには、酸添加の調
整によつて、酸度および風味を調整でき、種々のタイプ
の低アルコール濃度清酒をつくることができるものであ
る。また、実施例1と2を比較してわかるように、糖化
後の上槽は、味、風味には影響はあまりないが、後の工
程や製品の安定性から考えると、上槽した方がより好ま
しいといえる。
As described above, the present invention, after saccharification, by heating to inactivate enzymes to a certain extent or more, and by separating saccharification and fermentation, a product without ig taste that causes tiredness in drinking is obtained. It can be easily manufactured. Furthermore, the acidity and flavor can be adjusted by adjusting the acid addition, and various types of low alcohol concentration sake can be prepared. Further, as can be seen by comparing Examples 1 and 2, the upper tank after saccharification has little influence on taste and flavor, but considering the subsequent steps and the stability of the product, the upper tank is better. It can be said that it is more preferable.

これら本発明製品の効果は、糖化と発酵を加熱失活によ
つて分離することで得られるものである。
These effects of the product of the present invention are obtained by separating saccharification and fermentation by heat inactivation.

(実施例) 実施例1 総米 20kg 蒸米 15kg 麹米 5kg 汲水 40 乳酸 180g 水40に麹米5kgおよび蒸米15kgを加え、55℃に温度を
上げ、一昼夜糖化を行つた。その後、70℃に温度を上
げ、酵素活性を失活させ、上槽をせずにそのまま、それ
を15℃に落とし、7号酵母と乳酸180gを添加し常温で発
酵を行つた。7日目に一部を取つた。その時、(1)ア
ルコール分7.2%、(2)日本酒度−74、(3)酸度6.9
%であつた。14日目に残りを上槽した。そのとき、
(1)アルコール分9.8%、(2)日本酒度−20、
(3)酸度7.2%であつた。
(Example) Example 1 Total rice 20 kg Steamed rice 15 kg Koji rice 5 kg Pumped water 40 Lactic acid 180 g Water 40 was added with 5 kg of koji rice and 15 kg of steamed rice, and the temperature was raised to 55 ° C. to saccharify overnight. After that, the temperature was raised to 70 ° C. to deactivate the enzyme activity, the temperature was lowered to 15 ° C. without adding the upper tank, and yeast No. 7 and 180 g of lactic acid were added and fermentation was carried out at room temperature. I took a part on the 7th day. At that time, (1) alcohol content 7.2%, (2) sake degree -74, (3) acidity 6.9
It was in%. On the 14th day, the rest was placed in the upper tank. then,
(1) Alcohol content 9.8%, (2) Sake degree -20,
(3) The acidity was 7.2%.

実施例2 実施例1と同様の仕込配合で糖化を行い、上槽した後、
70℃に温度を上げ、酵素活性を失活させて所定の糖化液
を得た。この糖化液を15℃に下げ、7号酵母と乳酸100g
を添加し、常温で発酵を行つた。10日目に一部を取り
過を行つた。そのとき、(1)アルコール分7.4%、
(2)日本酒度−60、(3)酸度7.2%であつた。18日
目に残りを過した。そのとき、(1)アルコール分9.
5%、(2)日本酒度−18、(3)酸度7.4%であつた。
Example 2 After saccharification was carried out with the same preparation as in Example 1 and the upper tank was placed,
The temperature was raised to 70 ° C to deactivate the enzyme activity to obtain a predetermined saccharified solution. This saccharified solution is lowered to 15 ℃, and yeast 7 and lactic acid 100g
Was added and fermentation was carried out at room temperature. On the 10th day, a part was overtaken. At that time, (1) alcohol content 7.4%,
(2) Sake degree was -60, and (3) Acidity was 7.2%. I had the rest on the 18th day. At that time, (1) alcohol content 9.
5%, (2) Sake degree-18, and (3) Acidity 7.4%.

実施例3 実施例2と同様の操作で得た糖化液を用い、この糖化液
の温度を25℃に調整し、ワイン酵母と乳酸180gを添加
し、常温で発酵を行つた。7日目に一部を取り、過を
行つた。そのとき、(1)アルコール分6.2%、(2)
日本酒度−68、(3)酸度7.4%であつた。16日目に残
りを過した。そのとき、(1)アルコール分9.4%、
(2)日本酒度−21、(3)酸度7.8%であつた。
Example 3 Using the saccharified solution obtained in the same manner as in Example 2, the temperature of the saccharified solution was adjusted to 25 ° C., wine yeast and 180 g of lactic acid were added, and fermentation was carried out at room temperature. I took a part of it on the 7th day and went for a pass. At that time, (1) alcohol content 6.2%, (2)
The degree of sake was -68 and the acidity of (3) was 7.4%. I had the rest on the 16th day. At that time, (1) alcohol content 9.4%,
(2) Sake degree-21 and (3) acidity 7.8%.

実施例4 実施例2と同様の操作で得た糖化液を用い、その糖化液
を20℃に調整し、9号酵母と乳酸180gを添加し、常温で
発酵を行つた。7日目に一部を取り、過を行つた。こ
のとき、(1)アルコール分6.4%、(2)日本酒度−7
0、(3)酸度6.7%であつた。16日目に残りを過し
た。このとき、(1)アルコール分9.6%、(2)日本
酒度−20、(3)酸度7.4%であつた。
Example 4 Using the saccharified solution obtained by the same operation as in Example 2, the saccharified solution was adjusted to 20 ° C., No. 9 yeast and 180 g of lactic acid were added, and fermentation was carried out at room temperature. I took a part of it on the 7th day and went for a pass. At this time, (1) alcohol content 6.4%, (2) sake degree -7
0, (3) Acidity was 6.7%. I had the rest on the 16th day. At this time, (1) alcohol content was 9.6%, (2) sake degree was -20, and (3) acidity was 7.4%.

実施例5 実施例2と同様の操作で得た糖化液を用い、その糖化液
を20℃に調整し、7号酵母を添加し、常温で発酵を行つ
た。乳酸は添加しなかつた。7日目に一部を取り、過
を行つた。このとき、(1)アルコール分7.6%、
(2)日本酒度−58、(3)酸度3.0%であつた。16日
目に残りを過した。このとき、(1)アルコール分9.
8%、(2)日本酒度−18、(3)酸度3.1%であつた。
Example 5 Using the saccharified liquid obtained by the same operation as in Example 2, the saccharified liquid was adjusted to 20 ° C., No. 7 yeast was added, and fermentation was carried out at room temperature. No lactic acid was added. I took a part of it on the 7th day and went for a pass. At this time, (1) alcohol content 7.6%,
(2) Sake degree was -58 and (3) acidity was 3.0%. I had the rest on the 16th day. At this time, (1) alcohol content 9.
8%, (2) sake degree-18, and (3) acidity 3.1%.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】米、米麹を用いて糖化した後、そのままあ
るいは上槽してから加熱し、酵素を失活させて糖化を終
了させ、これを多酸存在下あるいはそのまま発酵を行
い、低アルコール濃度の任意の時点で発酵を止め上槽す
ることを特徴とする低アルコール濃度清酒の製造法。
1. After saccharification with rice or rice koji, the saccharification is terminated by deactivating the enzyme by heating the saccharification as it is or after heating it in the upper tank. A method for producing sake having a low alcohol concentration, which comprises stopping fermentation at an arbitrary point of alcohol concentration and starting the upper tank.
JP13168685A 1985-06-19 1985-06-19 Method for producing sake with low alcohol concentration Expired - Lifetime JPH0685709B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13168685A JPH0685709B2 (en) 1985-06-19 1985-06-19 Method for producing sake with low alcohol concentration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13168685A JPH0685709B2 (en) 1985-06-19 1985-06-19 Method for producing sake with low alcohol concentration

Publications (2)

Publication Number Publication Date
JPS61289875A JPS61289875A (en) 1986-12-19
JPH0685709B2 true JPH0685709B2 (en) 1994-11-02

Family

ID=15063844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13168685A Expired - Lifetime JPH0685709B2 (en) 1985-06-19 1985-06-19 Method for producing sake with low alcohol concentration

Country Status (1)

Country Link
JP (1) JPH0685709B2 (en)

Cited By (1)

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Publication number Priority date Publication date Assignee Title
CN104911064A (en) * 2015-06-25 2015-09-16 绍兴文理学院 Brewing process of yellow rice wine

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Publication number Priority date Publication date Assignee Title
JP4044712B2 (en) * 2000-01-28 2008-02-06 大関株式会社 Production method of low-alcohol sake
JP2002238542A (en) * 2001-02-19 2002-08-27 Takara Holdings Inc Low alcohol sake and method for producing the same
JP3617039B2 (en) * 2002-02-04 2005-02-02 美少年酒造株式会社 Low alcohol alcohol production method and low alcohol alcohol
JP3608116B2 (en) * 2002-03-14 2005-01-05 独立行政法人酒類総合研究所 Production method of low-alcohol sake
JP3640946B2 (en) * 2002-09-27 2005-04-20 独立行政法人酒類総合研究所 Production method of sparkling low alcohol sake
JP3707615B2 (en) * 2003-03-25 2005-10-19 独立行政法人酒類総合研究所 Production method of low-alcohol sake
JP2005224176A (en) * 2004-02-13 2005-08-25 Kameda Shuzo Kk Method for producing wine-fashioned japanese sake with rice as main material
JP6834071B2 (en) * 2017-04-03 2021-02-24 天山酒造株式会社 How to make sparkling sake

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104911064A (en) * 2015-06-25 2015-09-16 绍兴文理学院 Brewing process of yellow rice wine

Also Published As

Publication number Publication date
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