JPH10276755A - Production of sake - Google Patents
Production of sakeInfo
- Publication number
- JPH10276755A JPH10276755A JP10836797A JP10836797A JPH10276755A JP H10276755 A JPH10276755 A JP H10276755A JP 10836797 A JP10836797 A JP 10836797A JP 10836797 A JP10836797 A JP 10836797A JP H10276755 A JPH10276755 A JP H10276755A
- Authority
- JP
- Japan
- Prior art keywords
- sake
- rice
- saccharified
- alcohol
- saccharified product
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title abstract description 22
- 235000007164 Oryza sativa Nutrition 0.000 claims abstract description 72
- 235000009566 rice Nutrition 0.000 claims abstract description 71
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 35
- 235000019640 taste Nutrition 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 4
- 241000209094 Oryza Species 0.000 claims abstract 13
- 238000000034 method Methods 0.000 claims description 27
- 238000005086 pumping Methods 0.000 claims description 26
- 238000002360 preparation method Methods 0.000 claims description 22
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 14
- 102000004190 Enzymes Human genes 0.000 claims description 13
- 108090000790 Enzymes Proteins 0.000 claims description 13
- 235000021329 brown rice Nutrition 0.000 claims description 8
- 235000014655 lactic acid Nutrition 0.000 claims description 7
- 239000004310 lactic acid Substances 0.000 claims description 7
- 239000002994 raw material Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 3
- 238000004898 kneading Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 31
- 240000004808 Saccharomyces cerevisiae Species 0.000 abstract description 17
- 239000007788 liquid Substances 0.000 abstract description 17
- 239000000243 solution Substances 0.000 abstract description 12
- 239000000203 mixture Substances 0.000 abstract description 11
- 239000007787 solid Substances 0.000 abstract description 5
- 239000007864 aqueous solution Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- 240000007594 Oryza sativa Species 0.000 description 59
- 239000000047 product Substances 0.000 description 42
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 22
- 239000008103 glucose Substances 0.000 description 22
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 16
- 241000894006 Bacteria Species 0.000 description 14
- 238000000855 fermentation Methods 0.000 description 14
- 230000004151 fermentation Effects 0.000 description 14
- 229940088598 enzyme Drugs 0.000 description 11
- 238000011109 contamination Methods 0.000 description 10
- 235000019647 acidic taste Nutrition 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 6
- 230000001580 bacterial effect Effects 0.000 description 5
- 238000005498 polishing Methods 0.000 description 5
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- 241000519695 Ilex integra Species 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000000543 intermediate Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 235000007189 Oryza longistaminata Nutrition 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 102000004139 alpha-Amylases Human genes 0.000 description 1
- 108090000637 alpha-Amylases Proteins 0.000 description 1
- 229940024171 alpha-amylase Drugs 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 235000013405 beer Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 235000013681 dietary sucrose Nutrition 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000005360 mashing Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000012258 stirred mixture Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229960004793 sucrose Drugs 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 235000015041 whisky Nutrition 0.000 description 1
- 235000020985 whole grains Nutrition 0.000 description 1
Landscapes
- Alcoholic Beverages (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、蒸米を原料とする
糖化物、それを使用する清酒の製造方法に関するもので
あり、この糖化物を使用することにより、淡白な味から
濃醇な味までの幅広い酒質の清酒を効率的に工業生産す
ることができる。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a saccharified product using steamed rice as a raw material and a method for producing sake using the saccharified product. Can efficiently produce industrial sake with a wide range of sake qualities.
【0002】[0002]
【従来の技術】清酒醸造用の醪は、通常、蒸米、麹及び
水が同時に仕込まれ、蒸米の溶解、糖化、酵母の増殖及
びアルコール発酵が同時に進行する。これは並行複発酵
と呼ばれる優れた方法であるが、醪中において蒸米の溶
解、糖化、酵母の増殖及びアルコール発酵が別個に制御
できないこと、清酒の醪は汲水歩合が120ないし14
0%程度の仕込みであるが、仕込初期において醪の流動
性が低く温度の制御ができないこと等の問題点がある。2. Description of the Prior Art Steamed rice, koji and water are usually charged simultaneously in sake brewing mash, and dissolution of steamed rice, saccharification, yeast growth, and alcohol fermentation proceed simultaneously. This is an excellent method called parallel compound fermentation, but the dissolution of steamed rice, saccharification, yeast growth and alcohol fermentation cannot be controlled separately in the mash, and sake mash has a pumping rate of 120 to 14
Although the preparation is about 0%, there is a problem that the flowability of the mash is low at the initial stage of the preparation and the temperature cannot be controlled.
【0003】これに対して、ビールやウイスキーは、糖
化液を製造した後発酵を行ういわゆる単発酵により製造
されている。清酒醸造においても単発酵が検討されてき
たが、糖化液を醪に添加したとき、醪のグルコース濃度
が高い場合は酵母の増殖及びアルコール発酵が阻害され
ること、糖化液が雑菌に汚染されやすいこと、糖化液の
製造が煩雑であること等の問題点がある。濃糖による影
響を避けるため、汲水歩合約260ないし430%程度
で米を糖化し発酵を行う清酒の製造法が検討された(醸
造協会誌、81(6) p.402−408(198
6))が、このような高い汲水歩合では普通酒のような
濃醇な清酒を製造することはできない。On the other hand, beer and whiskey are produced by so-called simple fermentation in which a saccharified liquid is produced and then fermented. Single fermentation has also been studied in sake brewing, but when saccharified liquid is added to mash, if the glucose concentration of the mash is high, yeast growth and alcohol fermentation are inhibited, and the saccharified liquid is easily contaminated by various bacteria And that the production of the saccharified solution is complicated. In order to avoid the influence of concentrated sugar, a method of producing sake that saccharifies and ferments rice at a pumping rate of about 260 to 430% has been studied (Journal of the Brewing Association, 81 (6) p. 402-408 (198).
6)), but at such a high pumping rate, it is not possible to produce rich sake like ordinary sake.
【0004】一方、清酒醸造においては、通常の総米に
対する汲水歩合である120ないし140%よりも濃厚
な仕込みは酒母において行われているだけである。生も
と系酒母の汲水歩合は、103%前後であって清酒製造
においては最も濃厚な仕込み方法であるが、汲水が少な
いため蒸米を溶解させるのが困難であり、櫂ですりつぶ
す(生もと)、仕込容器の底にたまった液を汲み出して
蒸米に振りかける(汲掛)、湯をつめた容器を使って部
分的に加温する(暖気操作)等の特殊な方法が採られ
る。現在、清酒製造において米の糖化液を使用する場合
は、糖化操作及び糖化液のグルコース濃度を勘案して汲
水歩合は150ないし200%程度とするのが普通であ
り、雑菌による汚染を避けるため製造後直ちに使用され
ている。[0004] On the other hand, in sake brewing, mashing is only carried out at a sake brewer whose concentration is higher than 120 to 140%, which is a normal water pumping rate for whole rice. Originally, the percentage of squeezed water from a sake brewer is around 103%, which is the most concentrated method in sake production. However, since the amount of squeezed water is small, it is difficult to dissolve steamed rice. Original method), a special method such as pumping out the liquid accumulated at the bottom of the brewing container and sprinkling it on steamed rice (pumping) or partially heating using a container filled with hot water (warming operation) is adopted. At present, when a saccharified liquid of rice is used in sake production, the pumping rate is usually about 150 to 200% in consideration of the saccharification operation and the glucose concentration of the saccharified liquid. Used immediately after production.
【0005】最近、汲水歩合120ないし125%と
し、α−アミラーゼによる粉砕した白米の液化液を掛米
として清酒製造に使用する方法(特公平2−3819
5)や汲水歩合170%程度で白米を蒸煮した後液化酵
素で液化した液を用いて発酵させる方法(醸造協会誌、
88(10) 756−762(1993))等液化酵
素を用いて米を液化して清酒を製造する方法が開発され
た。これらの方法は、最初に液化のみを行い麹で糖化さ
せながら発酵を行うこと、麹以外に多量の液化酵素を使
う必要があること、液化液製造時の汲水歩合は通常の清
酒醸造法または糖化液製造法の範疇内であること、液化
液は雑菌に汚染されやすいこと等から、本発明とは全く
別の技術である。[0005] Recently, a method of using a liquefied liquid of white rice pulverized by α-amylase with a pulp yield of 120 to 125% and using it as sake rice for sake production (Japanese Patent Publication No. 2-3819)
5) or a method of steaming white rice at a pumping rate of about 170% and then fermenting using a liquid liquefied with liquefied enzymes (Journal of the Brewing Association,
88 (10) 756-762 (1993)) A method for producing sake by liquefying rice using a liquefying enzyme has been developed. In these methods, only liquefaction is performed first and fermentation is performed while saccharifying with koji, it is necessary to use a large amount of liquefied enzyme other than koji, the pumping rate at the time of liquefied liquid production is the usual sake brewing method or This technology is completely different from the present invention because it is within the category of the saccharified liquid production method and the liquefied liquid is easily contaminated by various bacteria.
【0006】なお、清酒醪の留仕込において汲水の一部
に清酒を使用し留仕込直後の醪中のアルコール濃度を9
%程度として濃醇な清酒を製造する方法(醸造協会誌、
71(6) 469−475(1976))があるが、
本法と比較すると、清酒の添加時期、アルコール濃度及
び使用目的(本法の清酒使用目的は雑菌汚染防止であ
る)等の点で異なり、本発明とは全く別の技術である。[0006] In addition, during the preparation of sake mash, sake is used as a part of the pumped water, and the alcohol concentration in the mash immediately after the preparation is reduced to 9%.
% To produce rich sake (Brewery Association magazine,
71 (6) 469-475 (1976)),
Compared with the present method, the method is completely different from the present invention because it differs in the timing of adding sake, the alcohol concentration, and the purpose of use (the purpose of using sake in this method is to prevent bacterial contamination).
【0007】[0007]
【発明が解決しようとする課題】本発明は、このような
技術の現状に鑑み、清酒を単に効率的に製造するのでは
なく、各種目的とする清酒を自由に且つ効率的に工業生
産するシステムを新規に開発する目的でなされたもので
ある。SUMMARY OF THE INVENTION In view of the state of the art, the present invention provides a system for free and efficient industrial production of sake for various purposes, rather than simply producing sake. Was developed for the purpose of newly developing
【0008】[0008]
【課題を解決するための手段】本発明者らは、上記に設
定した新規な技術課題を解決するために検討した結果、
発想を転換して、化学合成法における中間体に着目し、
蒸米、麹、少量の清酒(アルコール水溶液)を混合して
糖化を行い、液状〜半固体状の糖化物を得た。Means for Solving the Problems The present inventors have studied to solve the above-mentioned new technical problem,
Changing the way of thinking, focusing on intermediates in chemical synthesis,
Saccharification was performed by mixing steamed rice, koji, and a small amount of sake (aqueous alcohol) to obtain a liquid to semi-solid saccharified product.
【0009】そしてこの糖化物を常法にしたがって処理
したところ、すぐれた酒母、醪が効率的に製造できると
いう有用新知見が得られ、しかも糖化物の組成を変化さ
せることによりそれに応じて各種の酒質の清酒が自由に
製造できるという有用新知見も更に得られ、この糖化物
が清酒製造用のすぐれた原料(中間体的原料)となるこ
とを確認し、更に研究の結果、本発明を完成するに至っ
た。[0009] When this saccharified product is treated according to a conventional method, useful new knowledge that an excellent sake liquor and mash can be produced efficiently can be obtained. In addition, by changing the composition of the saccharified product, various types of saccharified product can be obtained. The useful new knowledge that the sake of sake quality can be freely produced has been further obtained, and it has been confirmed that this saccharified product is an excellent raw material (intermediate raw material) for the production of sake. It was completed.
【0010】本発明においては、基本的には、蒸米、麹
(清酒用酵素剤)を原料とし、汲水歩合を低くして(6
0%以下、好ましくは50%以下)糖化を行い、液状〜
半固体状の糖化物を得、このようにして得られた糖化物
を用いて清酒を製造するものであり、雑菌による汚染を
特に防止したい場合には、糖化工程を、アルコールの存
在下、乳酸の存在下、及び/又は、嫌気条件下で実施す
るものである。とりわけ、糖化物の製造において、蒸
米、麹(清酒用酵素剤)、及び、少量の清酒(アルコー
ル水溶液)を用いて糖化処理を行う場合には、清酒(ア
ルコール水溶液)が汲水とアルコールの給源にもなり、
好適な態様のひとつとして推奨される。In the present invention, basically, steamed rice and koji (enzyme for sake) are used as raw materials, and the pumping rate is reduced (6).
0% or less, preferably 50% or less)
A semi-solid saccharified product is obtained, and sake is produced using the saccharified product thus obtained.If it is desired to particularly prevent contamination by various bacteria, the saccharification process is performed in the presence of alcohol using lactic acid. And / or under anaerobic conditions. In particular, in the case of saccharification, when saccharification is performed using steamed rice, koji (enzyme for sake), and a small amount of sake (aqueous alcohol), the sake (alcohol aqueous solution) is used as a source of pumping water and alcohol. Become
It is recommended as one of the preferred embodiments.
【0011】このように、本発明は、糖化方法、雑菌汚
染対策、及び発酵方法の各要件にそれぞれ特徴を有する
だけでなく、これらの有機的結合にも特徴を有するもの
である。以下、本発明について具体的に詳述する。As described above, the present invention not only has a feature in each requirement of a saccharification method, a countermeasure against various bacteria, and a fermentation method, but also has a feature in an organic bond thereof. Hereinafter, the present invention will be described in detail.
【0012】[0012]
【発明の実施の形態】先ず、糖化方法について述べる。
本発明においては、汲水歩合が60%以下、好ましくは
50%以下と、極度に低く、したがって、仕込んで数時
間経つと、水は蒸米に吸収されて液部はほとんどなくな
るような状態となり、糖化は極めて困難である。このよ
うな状態のものを糖化するには、実施例1に示すように
すりつぶした後、麹を混和すると効果的である。DESCRIPTION OF THE PREFERRED EMBODIMENTS First, a saccharification method will be described.
In the present invention, the pumping rate is extremely low, such as 60% or less, preferably 50% or less. Therefore, after several hours of charging, the water is absorbed by steamed rice, and the liquid portion almost disappears. Saccharification is extremely difficult. In order to saccharify such a state, it is effective to grind as shown in Example 1 and then to mix koji.
【0013】具体的には、蒸米に5ないし50%の水を
加えて混練し、餅状又はのり状となったものに麹を加え
てよく混合し、55℃程度で10ないし24時間程度保
持するか、室温(15ないし20℃程度)で6日間程度
保持すれば糖化が進行し、液状または半固体状の甘みの
強い糖化物になる。室温の場合糖化は徐々に進行し長く
おくほど糖化は進行する。55℃程度に保持すると糖化
は速く進行するが、物量が多い場合は、温度が上昇しに
くいので加温器を使って部分的に加温する必要がある。
仕込みが大量の場合には、すりつぶすのは困難なので、
実施例4に示すように、玄米または白米を蒸した後圧砕
または破砕し、麹及び少量の水と混和し糖化を進めれば
よい。なお、糖化時に55℃程度とした後冷却すれば酵
素は残存しているので、酒母または醪を仕込んだ後溶解
及び糖化はさらに進行する。仕込む時点でグルコース濃
度が15%程度以上あれば水で希釈して醪に仕込んだと
き十分流動性はあるので、蒸米は完全に糖化が終了して
いなくてもよい。More specifically, 5 to 50% of water is added to kneaded steamed rice and kneaded, and koji is added to the rice cake or glue, and the mixture is mixed well and kept at about 55 ° C. for about 10 to 24 hours. Alternatively, if the saccharification is maintained at room temperature (about 15 to 20 ° C.) for about 6 days, the saccharification proceeds, and the saccharified product becomes a liquid or semi-solid, highly sweet saccharified product. At room temperature, the saccharification progresses gradually, and the saccharification progresses as the length increases. Saccharification proceeds rapidly when the temperature is maintained at about 55 ° C., but when the amount is large, the temperature does not easily rise, so that it is necessary to partially heat using a warming device.
If the preparation is large, it is difficult to grind,
As shown in Example 4, brown rice or white rice is steamed, then crushed or crushed, mixed with koji and a small amount of water, and saccharification may be advanced. If the temperature is reduced to about 55 ° C. at the time of saccharification and then cooled, the enzyme remains, so that the dissolving and saccharification further proceed after charging the sake mash or moromi. If the glucose concentration is about 15% or more at the time of charging, the saccharification of the steamed rice does not have to be completely completed because the liquid has sufficient fluidity when diluted with water and charged into the mash.
【0014】次に、雑菌汚染対策について述べる。水分
活性が62以下であれば、ほとんどの微生物が生育しな
い(食品微生物学ハンドブック、p.75、技報堂出版
(株)、1995)とされているが、仕込み直後のグル
コース濃度が低いときには雑菌に汚染される場合があ
り、例えば本発明においても、実施例1において汲水歩
合が20%以上の仕込区分において野生酵母が検出さ
れ、汲水歩合30%以上の仕込区分において酢酸エチル
様の香りが発生したが、これは好気性の産膜酵母に汚染
されたためと推察された。そこで実施例4に示すよう
に、糖化容器を密閉し、空気との接触をなるべく避ける
ため攪拌を行わなかった仕込区分は、野生酵母の増殖を
抑えることができ、細菌酸度も低かった。したがって、
嫌気的な条件で糖化を進めれば雑菌による汚染は防止で
きることが確認されたが、本法を産業的に利用するため
には、さらに安全性を高める必要性を認めた。Next, countermeasures against various bacteria will be described. If the water activity is 62 or less, most microorganisms do not grow (Food Microbiology Handbook, p. 75, Gihodo Shuppan Co., Ltd., 1995). For example, in the present invention, for example, in Example 1, wild yeast is detected in the preparation section where the pumping rate is 20% or more, and an ethyl acetate-like scent is generated in the preparation section where the pumping rate is 30% or more. However, this was presumed to be due to contamination by aerobic membrane-producing yeast. Thus, as shown in Example 4, in the preparation section in which the saccharification vessel was sealed and stirring was not performed to avoid contact with air as much as possible, the growth of wild yeast could be suppressed and the bacterial acidity was low. Therefore,
It has been confirmed that contamination by various bacteria can be prevented if saccharification is promoted under anaerobic conditions. However, in order to use this method industrially, it was necessary to further increase the safety.
【0015】そのため、乳酸処理を行うこととし、例え
ば55℃程度で糖化した後に乳酸を添加する方法は有力
であるが、糖化物の粘度が高いために混和が困難であっ
たり、乳酸の使用によって醪酸度の増加がもたらされた
りする場合が生じる。For this reason, a method of adding lactic acid after saccharification at about 55 ° C. is effective, for example, in which lactic acid treatment is performed. However, mixing is difficult due to the high viscosity of the saccharified product, In some cases, the acidity of the mash is increased.
【0016】そこで、このような場合には、実施例5に
示すように、水の代わりに清酒またはアルコール水溶液
を利用し、アルコールの存在下で糖化を行うと雑菌の増
殖を防止するのに有効であることが分かった。本法にお
いて雑菌による主な汚染源は麹であるから、麹を蒸米に
混和する前に清酒またはアルコール水溶液に浸漬してお
けば酵素の抽出と殺菌が行われ有効である。糖化物中の
アルコール濃度は雑菌汚染防止の点からは濃度が高い方
が効果は高いが、多量の清酒またはアルコールの使用は
製造コストの上昇につながり、またアルコール濃度があ
まり高ければ発酵阻害ともなる。実施例5に示すように
3%程度以上のアルコール存在下で糖化を行えば糖化反
応は阻害されず、雑菌の汚染防止に効果があることが分
かった。したがって、糖化工程及び糖化物保存中の雑菌
による汚染防止策としては、グルコース濃度が高くなる
ように汲水歩合を低くすると共に、3%程度以上好適に
は5%以上のアルコール存在下で密閉して糖化を行い、
糖化終了後は密閉して保存することはきわめて効果的で
あることが分かった。In such a case, as shown in Example 5, using sake or alcohol aqueous solution instead of water and saccharification in the presence of alcohol is effective in preventing the growth of various bacteria. It turned out to be. In this method, koji is the main source of contamination by various bacteria, so if the koji is immersed in sake or alcoholic water before being mixed with steamed rice, the extraction and sterilization of enzymes will be effective. The higher the alcohol concentration in saccharified products, the higher the concentration from the viewpoint of preventing bacterial contamination, but the use of a large amount of sake or alcohol leads to an increase in production costs, and if the alcohol concentration is too high, it also inhibits fermentation. . As shown in Example 5, when saccharification was performed in the presence of about 3% or more of alcohol, the saccharification reaction was not inhibited, and it was found that the saccharification reaction was effective in preventing contamination of various bacteria. Therefore, as a measure for preventing contamination by germs during the saccharification process and saccharified product storage, the pumping rate is reduced so that the glucose concentration is increased, and the container is sealed in the presence of about 3% or more, preferably 5% or more of alcohol. Saccharification,
After the saccharification was completed, it was found that it was extremely effective to store in a sealed state.
【0017】そして、発酵方法について述べる。清酒酵
母はグルコース濃度が非常に高い場合は増殖及びアルコ
ール発酵が阻害され、グルコース濃度が非常に低い場合
はアルコール生産が停滞することが知られている。本法
によって製造した糖化物を用いて酒母または醪を製造す
る場合は、発酵液中のグルコース濃度を用途に応じ5な
いし25%程度の範囲内に制御することが重要である。Next, the fermentation method will be described. Sake yeast is known to inhibit growth and alcohol fermentation when the glucose concentration is very high, and to stagnate alcohol production when the glucose concentration is very low. When mash or mash is produced using the saccharified product produced by this method, it is important to control the glucose concentration in the fermentation liquor within a range of about 5 to 25% depending on the application.
【0018】酒母を製造する場合は、原料米に対し汲水
歩合130ないし150%程度となるように糖化物に水
を加え、さらに乳酸と酵母を添加し、通常の高温糖化酒
母と同様に育成すればよい。ただし、糖化物のグルコー
ス濃度が高い場合は、酒母仕込後のグルコース濃度が2
5%程度以下となるよう加水する。In the case of producing sake brewer, water is added to the saccharified product so that the pumping rate is about 130 to 150% based on the raw rice, lactic acid and yeast are further added, and the cultivation is carried out in the same manner as ordinary high temperature saccharified brewery. do it. However, if the glucose concentration of the saccharified product is high, the glucose concentration
Water is added so as to be about 5% or less.
【0019】醪は、目的とする清酒のタイプにより製造
方法が異なるが、いずれの場合も糖化物と水の混和物
(以後掛用糖化液という)を酒母または醪に添加した後
の醪中のグルコース濃度は20%程度以下望ましくは1
5%程度以下とすること、糖化物を醪に添加する前の醪
中のグルコース濃度は2%程度以上望ましくは5%程度
以上あることが重要である。濃醇な味の清酒を製造する
場合は、上述の範囲内で濃厚な掛用糖化液を調整し醪に
添加すればよく、また淡白な味の清酒またはアルコール
濃度の低い清酒を製造する場合は、水を多く加えた掛用
糖化液を調製して醪に添加すればよい。The method of producing moromi differs depending on the type of sake that is desired. In any case, a mixture of saccharified product and water (hereinafter referred to as a saccharified solution for hanging) is added to the sake liquor or moromi. The glucose concentration is about 20% or less, preferably 1
It is important that the concentration is about 5% or less, and that the glucose concentration in the mash before adding the saccharified product to the mash is about 2% or more, preferably about 5% or more. When producing sake with a rich taste, a thick saccharified solution for hanging can be prepared and added to the mash within the above range, and when producing sake with a pale taste or sake with a low alcohol concentration, Then, a saccharified solution for hanging with a large amount of water may be prepared and added to the mash.
【0020】醪を製造する場合は、まず初添として酒母
の重量の50ないし100%程度の掛用糖化液を酒母に
加え、所定の発酵温度に保つ。グルコース濃度があらか
じめ定めた下限値例えば5%まで低下したら、二掛とし
て更に掛用糖化液を加える。以後、予定した醪量に達す
るまで同様の操作を行う。一度に醪に添加する掛用糖化
液量は醪中の酵母密度の低下を避けるため、醪重量の1
00%程度以下とするのが望ましい。In the case of producing moromi, a saccharified solution for hanging, which is about 50 to 100% of the weight of the sake brewer, is first added to the sake brewer and kept at a predetermined fermentation temperature. When the glucose concentration falls to a predetermined lower limit, for example, 5%, a saccharified solution for hanging is added as a double hook. Thereafter, the same operation is performed until the expected amount of mash is reached. The amount of saccharified solution added to the mash at a time is 1% of the mash weight in order to avoid a decrease in yeast density in the mash.
It is desirable to set it to about 00% or less.
【0021】上記したように、本発明に係る糖化物は、
蒸米及び麹(清酒用酵素剤)を原料として製造するもの
であるが、蒸米としては、モチ米、ウルチ米の精白米
(精米歩合は適宜変化させることができる)、玄米を使
用することができ、また、粒面の全部又は一部が着色し
た粒、及び赤米を包含する着色米も使用することができ
る。更に必要あれば、これらの混合物も使用可能であ
る。As described above, the saccharified product according to the present invention comprises:
It is manufactured using steamed rice and koji (enzyme agent for sake) as raw materials. As steamed rice, mochi rice, polished rice of ulch rice (the ratio of polished rice can be changed as appropriate), and brown rice can be used. Also, colored rice including all or part of the grain surface colored and red rice can be used. If necessary, these mixtures can also be used.
【0022】本発明において、蒸米は、破砕したもの、
圧砕したもの、及び/又は、混練したものがいずれも使
用可能であり、屑米や餅状としたものも使用することが
できる。もちろん、このような処理をすることのない粒
子状の蒸米も使用することができる。In the present invention, steamed rice is crushed,
Any of crushed and / or kneaded materials can be used, and crushed rice or rice cake-shaped products can also be used. Of course, particulate steamed rice that does not undergo such treatment can also be used.
【0023】また、全粒、破砕、圧砕した生米を蒸して
得た蒸米も、同様に使用することができる。Also, steamed rice obtained by steaming whole grain, crushed and crushed raw rice can be used in the same manner.
【0024】以下、本発明を実施例に基づき更に詳細に
説明する。Hereinafter, the present invention will be described in more detail with reference to examples.
【0025】[0025]
【実施例1:蒸米を餅状にする糖化物の製造】モチ米
(精米歩合90%程度)と乾燥麹(にしほまれ、精米歩
合70%、水分5.95%)を用い、麹歩合は33.3
%、汲水歩合は10ないし50%として糖化物製造試験
を行った。仕込配合は、表1のとおりであった。[Example 1] Production of saccharified product to make steamed rice into rice cake-like product Using mochi rice (about 90% of rice polishing rate) and dried koji (70% of rice polishing rate, water of 5.95%), koji percentage is 33.3
% And the pumping rate was 10 to 50%, and the saccharified product production test was performed. The charge composition was as shown in Table 1.
【0026】[0026]
【表1】 [Table 1]
【0027】浸漬、水切りは各2時間、蒸し時間は30
分間であった。蒸し上がったモチ米を餅つき器で餅状と
してから5等分し、50℃以下になってから、それぞれ
に前もって所定量の水を加えておいた麹を加えてよく混
合した後、それぞれを仕込容器に入れ室温(26℃)に
約18時間放置、その後15℃の恒温室に移した。1日
1回攪拌し、分析用試料を採取した。グルコース濃度が
変化しなくなった時、5℃の恒温室に移した。分析方法
はグルコースは酵素法(グルコースBテストワコー)、
ブリックスはデジタル糖度計((株)アタゴ製PR−1
00)、ボーメは振動式密度比重計(京都電子工業
(株)製、DA−300)、酸度・アミノ酸度は国税庁
所定分析法によった。Dipping and draining are each 2 hours, and steaming time is 30 hours.
Minutes. The steamed rice cake is divided into 5 pieces by using a rice cake sticker and then divided into 5 equal parts. After the temperature reaches 50 ° C or lower, koji to which a predetermined amount of water has been added in advance is added and mixed well. The mixture was placed in a charging container, left at room temperature (26 ° C.) for about 18 hours, and then transferred to a 15 ° C. constant temperature room. The mixture was stirred once a day, and a sample for analysis was collected. When the glucose concentration stopped changing, it was moved to a 5 ° C constant temperature room. The analysis method is glucose enzymatic method (glucose B test wako),
Brix is a digital refractometer (PR-1 manufactured by Atago Co., Ltd.)
00), Baume was a vibratory density meter (DA-300, manufactured by Kyoto Electronics Industry Co., Ltd.), and the acidity and amino acid content were determined by the National Tax Agency specified analysis method.
【0028】仕込んで5日目の糖化物の分析値を表2に
示した。グルコース濃度は19.1〜20.4%とな
り、汲水の少ない方がグルコース濃度は高かった。生酸
菌及び野生酵母については、細菌酸度の測定及びTTC
法による野生酵母の検出を行った。細菌酸度はいずれも
ブランク以下で生酸菌により汚染されていないと考えら
れた(表3)。TTC培地にはピンクに染色される野生
酵母が表4のように汲水歩合の高い方に多く出現した。Table 2 shows the analytical values of the saccharified product on the 5th day after charging. The glucose concentration was 19.1 to 20.4%, and the glucose concentration was higher when the amount of the pumped water was smaller. For acid-fast bacteria and wild yeast, measurement of bacterial acidity and TTC
Wild yeast was detected by the method. All of the bacterial acidities were below the blank and considered not to be contaminated by live acid bacteria (Table 3). In the TTC medium, many wild yeasts stained pink appeared at higher pumping rates as shown in Table 4.
【0029】[0029]
【表2】 [Table 2]
【0030】[0030]
【表3】 [Table 3]
【0031】[0031]
【表4】 [Table 4]
【0032】下記表5に示すように5日目の糖化物は仕
込区分A、B及びCについてわずかに酢酸エチル様の香
りが感じられた。これは産膜酵母による汚染と推察され
た。したがって、本法においては生酸菌とともに産膜酵
母に対する対策が必要と考えられた。As shown in Table 5 below, the saccharified product on the 5th day had a slightly ethyl acetate-like scent in the charging categories A, B and C. This was presumed to be contamination by the membrane-forming yeast. Therefore, in this method, it was considered necessary to take measures against the membrane-producing yeast together with the acid-fast bacteria.
【0033】[0033]
【表5】 [Table 5]
【0034】[0034]
【実施例2:モチ米を使用した糖化物による酒母の製
造】実施例1で製造したそれぞれの糖化物の14%(白
米・麹の84g相当)を取り、汲水歩合150%になる
ように水を加え、汲水の0.72%に相当する乳酸を加
えた。容量1Lのガラス製容器に糖化物、水、乳酸及び
酵母(協会7号)を加え、15℃の恒温水槽内に浸し以
後、15℃一定とした。酒母の経過例として仕込区分A
について表6に示した。小仕込みであるため成分につい
てはブリックスのみ測定した。品温は各容器共ほぼ等し
かった。使用前酒母(仕込後8日目)の分析結果を表7
に示した。使用時までにボーメが切れてしまったが成
分、香り等に異常はなかった。Example 2: Production of Sake with Saccharified Products Using Mochi Rice 14% of each of the saccharified products produced in Example 1 (corresponding to 84 g of white rice and koji) was taken so that the pumping rate became 150%. Water was added and lactic acid equivalent to 0.72% of the water drawn. Saccharide, water, lactic acid, and yeast (Kyoto No. 7) were added to a glass container having a capacity of 1 L, immersed in a 15 ° C constant temperature water bath, and kept at 15 ° C. Preparation category A
Is shown in Table 6. Because of small preparation, only Brix was measured for the components. The product temperature was almost equal in each container. Table 7 shows the results of the analysis of the mother sake before use (8 days after preparation).
It was shown to. Baume had been cut by the time of use, but there was no abnormality in components, fragrance, etc.
【0035】[0035]
【表6】 [Table 6]
【0036】[0036]
【表7】 [Table 7]
【0037】[0037]
【実施例3:モチ米を使用した糖化物による醪仕込試
験】「掛用糖化液」は汲水歩合140%となるように糖
化物に水を加えて調整した。実施例2で製造した酒母2
00gを仕込容器に取り、初添として酒母と同重量の掛
用糖化液を加え、15℃に保ち、2日目以降は13℃と
した。二掛以後はグルコース濃度が5%以下になったと
き現在量の1/2量の掛用糖化液を加え、五掛まで行っ
た。図1には初添後12日目までの醪中のグルコース濃
度の測定例を仕込区分A、B及びCについて示した。ま
た、上槽後の清酒の分析値を表8に示したが、酸度とア
ミノ酸度の高い清酒となった。[Example 3: Morning preparation test using saccharified product using waxy rice] "Saccharified saccharified solution" was prepared by adding water to the saccharified product so that the pumping rate was 140%. Sake mother 2 produced in Example 2
Then, 00 g was placed in a charging container, and a saccharified solution for hanging with the same weight as the sake mother was added as an initial addition, and the temperature was kept at 15 ° C. and kept at 13 ° C. from the second day on. After the second batch, when the glucose concentration became 5% or less, a half of the current amount of the saccharified solution was added, and the process was performed up to five batches. FIG. 1 shows an example of measuring the glucose concentration in the mash up to 12 days after the initial addition for the charging categories A, B and C. In addition, the analysis values of the sake after the upper tank are shown in Table 8, but the sake has a high acidity and amino acid content.
【0038】[0038]
【表8】 [Table 8]
【0039】[0039]
【実施例4:玄米による糖化物の製造】玄米(日本晴)
と乾燥麹(にしほまれ、、精米歩合70%、水分5.9
5%)を用い麹歩合は33.3%、汲水歩合は30%と
した。玄米は約18時間浸漬し、2時間水切り、50分
間蒸した後、ローラーで圧砕し、あらかじめ所定量の水
に浸漬しておいた麹と混和した。仕込後15℃一定と
し、空気との接触を抑えるため密閉したものと、毎日1
回攪拌したものについて6日後に分析した。それぞれロ
ーラーで圧砕しないものを対照とした。[Example 4: Production of saccharified product using brown rice] Brown rice (Nipponbare)
And dried koji (Nishihomora, rice polishing rate 70%, moisture 5.9
5%), the koji ratio was 33.3%, and the pumping ratio was 30%. Brown rice was soaked for about 18 hours, drained for 2 hours, steamed for 50 minutes, crushed with a roller, and mixed with koji previously immersed in a predetermined amount of water. After the preparation, keep the temperature at 15 ° C and keep it tightly closed to prevent contact with air.
The agitated twice was analyzed after 6 days. Those not crushed by a roller were used as controls.
【0040】仕込後6日目の糖化物を遠心分離しその上
澄液の分析結果を表9に示した。遠心分離する前は粘度
の高い半固体状であったが遠心分離により10%前後の
上澄液が得られた。玄米もローラーで圧砕すれば糖化が
進行することから、これを用いて清酒醸造が可能と推察
された。攪拌しなかったものは攪拌したものに比べ野生
酵母の検出数が少なく、密閉した効果が認められた。The saccharified product 6 days after the preparation was centrifuged, and the analysis results of the supernatant were shown in Table 9. Before the centrifugation, the mixture was in a semi-solid state with a high viscosity, but a supernatant liquid of about 10% was obtained by centrifugation. If brown rice is also crushed with a roller, saccharification proceeds, so it was presumed that sake brewing was possible using this. Those that were not stirred had a smaller number of wild yeasts detected than those that were stirred, and the effect of sealing was observed.
【0041】[0041]
【表9】 [Table 9]
【0042】[0042]
【実施例5:ウルチ米を使用した糖化物製造におけるア
ルコールの影響】日本晴(精米歩合70%)と乾燥麹
(にしほまれ、、精米歩合70%、水分5.95%)を
用い麹歩合は23%、総米に対し0ないし5%(vo
l./wt.)のアルコールを含む水溶液を使用して汲
水歩合30及び50%とし、蒸米は圧砕せずに仕込み糖
化試験を行った。総米に対しアルコールを5%加えたと
き、仕込み直後のアルコール含量は約3%であった。仕
込後15℃一定とし、密閉し攪拌しないものと毎日1回
攪拌したものについて6日後に分析した。また、麹の代
わりに醪用酵素剤(コクラーゼ剣、日本資糧工業(株)
製)を総米の0.05%添加し、アルコールは総米の5
%、汲水歩合50%としたものについても同時に試験し
た。Example 5: Influence of alcohol on production of saccharified product using wurch rice: The koji ratio was determined using Nipponbare (rice polishing rate 70%) and dried koji (nishihokara, rice polishing rate 70%, water 5.95%). 23%, 0-5% (vo
l. / Wt. Using a water solution containing alcohol of (3), the pumping ratio was set to 30 and 50%, and the steamed rice was subjected to a saccharification test without crushing. When 5% alcohol was added to the whole rice, the alcohol content immediately after the preparation was about 3%. After the preparation, the temperature was kept constant at 15 ° C., and those after being sealed and not stirred and those stirred once a day were analyzed after 6 days. In addition, instead of koji, an enzyme agent for mash (Coclase Sword, Nippon Shokuhin Kogyo Co., Ltd.)
Is added at 0.05% of total rice, and alcohol is 5% of total rice.
% And a pumping rate of 50% were also tested.
【0043】実験結果は表10に示した。実験の範囲内
で糖化反応へのアルコールの影響は認められなかった。
6日間のグルコース生成量は表2及び表9の結果より低
かったが表10は麹歩合が23%と低いこと、混練また
は圧砕していないこと等が原因と推察された。麹の代わ
りに醪用酵素剤を使用した仕込区分は麹を使用した仕込
み区分よりグルコースの生成量が多く、この程度の汲水
歩合においても酵素剤が有効であることを確認した。酢
酸エチル様臭はアルコール添加量が少なく、かつ攪拌し
たものに発生したが、攪拌したものもアルコール添加量
が5%の仕込み区分については発生しなかった。また、
密閉したものはアルコールを添加しなかったものも酢酸
エチル様臭は発生しなかった。以上の結果から、蒸米と
麹の混合物はなるべく空気に触れないようにし、アルコ
ール3%程度以上の存在下で糖化すれば、雑菌に汚染さ
れることなく安全に糖化物を製造できることが確認され
た。The experimental results are shown in Table 10. No effect of alcohol on the saccharification reaction was observed within the experimental range.
The amount of glucose produced for 6 days was lower than the results in Tables 2 and 9, but Table 10 was presumed to be due to the low koji yield of 23% and the absence of kneading or crushing. It was confirmed that the amount of glucose produced in the preparation section using the enzyme preparation for mash instead of the koji was higher than that in the preparation section using koji, and that the enzyme preparation was effective even at such a rate of pumping. Ethyl acetate-like odor was generated in the case where the amount of alcohol added was small and the mixture was stirred. However, even in the case of the stirred mixture, no odor was generated in the charging section where the alcohol addition amount was 5%. Also,
Ethyl acetate-like odor was not generated in the sealed product without alcohol. From the above results, it was confirmed that if the mixture of steamed rice and koji was exposed to air as little as possible and saccharified in the presence of about 3% or more of alcohol, saccharified products could be produced safely without contamination by various bacteria. .
【0044】[0044]
【表10】 [Table 10]
【0045】[0045]
【発明の効果】以上説明したように、本発明によれば、
玄米または白米を用いて雑菌に汚染されることなく糖化
物を製造することができ、またこの糖化物を用いて仕込
初期から流動性の良い状態で酒母及び醪を製造すること
ができる。さらに、醪製造に当たっては糖化物の水によ
る希釈割合を変化させて醪に添加して発酵させることに
より濃醇な味から淡白な味までの清酒を製造することが
できる。As described above, according to the present invention,
Using brown rice or white rice, a saccharified product can be produced without being contaminated with various bacteria, and a saccharose and mash can be produced using the saccharified product in a state of good fluidity from the initial stage of preparation. Furthermore, in the production of mash, sake can be produced from a rich taste to a pale taste by changing the dilution ratio of the saccharified product with water and adding it to the mash for fermentation.
【0046】したがって、この糖化物を用意しておけ
ば、工業的大量生産に対応できることはもとより、希望
する酒質の清酒の製造にもキメ細かく対応することがで
きる。また、この糖化物の製造には、良質の酒造米のほ
か、品質の劣化した米、屑米等も使用でき、種類、形
状、品質、精白度等に応じて各種バラエティに富んだ糖
化物を製造することができる。Therefore, if this saccharified product is prepared, it is possible not only to cope with industrial mass production, but also to produce fine sake having a desired quality. For the production of this saccharified product, in addition to high-quality sake brewed rice, degraded rice and scrap rice can be used, and various types of saccharified products can be used depending on the type, shape, quality, and degree of milling. Can be manufactured.
【図1】醪中のグルコースの変化を示す。FIG. 1 shows changes in glucose in mash.
Claims (6)
剤を原料とし、アルコールの存在下、乳酸の存在下及び
/又は嫌気条件のもとにおいて、汲水歩合60%以下好
適には50%以下で糖化を行ってなる糖化物。1. A pumping rate of 60% or less, preferably 50% or less, in the presence of alcohol, lactic acid and / or anaerobic conditions, using steamed rice and an enzyme preparation for koji and / or sake. % Saccharified product obtained by saccharification at less than 10%.
に、汲水歩合60%以下、好適には50%以下に相当す
るとともに総米重量の3%以上好適には5%以上のアル
コールを含有する清酒又はアルコール水溶液、を原料と
し、これらを混合して糖化を行ってなる糖化物。2. An enzyme agent for steamed rice, koji and / or sake, and an alcohol corresponding to a pumping rate of 60% or less, preferably 50% or less, and 3% or more and preferably 5% or more of the total rice weight. A saccharified product obtained by using a sake or an aqueous alcohol solution containing the same as a raw material and mixing and saccharifying them.
を使用してなること、を特徴とする請求項1又は2に記
載の糖化物。3. The saccharified product according to claim 1, wherein polished rice, brown rice, or colored rice is used as the steamed rice.
は混練してなる蒸米を使用してなること、を特徴とする
請求項1〜3のいずれか1項に記載の糖化物。4. The saccharified product according to claim 1, wherein steamed rice obtained by crushing, crushing and / or kneading steamed rice is used as steamed rice.
化物を用いて酒母及び/又は醪を製造すること、を特徴
とする淡白な味から濃醇な味までの幅広い酒質の清酒を
製造する方法。5. A wide variety of sake qualities from pale taste to rich taste, characterized in that a saccharified product according to any one of claims 1 to 4 is used to produce a sake brewer and / or a mash. How to make sake.
酒。6. Sake produced by the method of claim 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10836797A JPH10276755A (en) | 1997-04-11 | 1997-04-11 | Production of sake |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10836797A JPH10276755A (en) | 1997-04-11 | 1997-04-11 | Production of sake |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10276755A true JPH10276755A (en) | 1998-10-20 |
Family
ID=14482974
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10836797A Pending JPH10276755A (en) | 1997-04-11 | 1997-04-11 | Production of sake |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10276755A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112646679A (en) * | 2020-12-30 | 2021-04-13 | 广东顺德酒厂有限公司 | Sake and its preparing method |
| JP2021193913A (en) * | 2020-06-11 | 2021-12-27 | 花の舞酒造株式会社 | Production method of sake |
| JP2023128906A (en) * | 2022-03-04 | 2023-09-14 | ニッカウヰスキー株式会社 | Moromi, alcoholic beverages and their manufacturing methods |
-
1997
- 1997-04-11 JP JP10836797A patent/JPH10276755A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2021193913A (en) * | 2020-06-11 | 2021-12-27 | 花の舞酒造株式会社 | Production method of sake |
| CN112646679A (en) * | 2020-12-30 | 2021-04-13 | 广东顺德酒厂有限公司 | Sake and its preparing method |
| CN112646679B (en) * | 2020-12-30 | 2022-11-22 | 广东顺德酒厂有限公司 | Sake and its preparing method |
| JP2023128906A (en) * | 2022-03-04 | 2023-09-14 | ニッカウヰスキー株式会社 | Moromi, alcoholic beverages and their manufacturing methods |
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