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JPH07298868A - Production of whisky - Google Patents

Production of whisky

Info

Publication number
JPH07298868A
JPH07298868A JP9676394A JP9676394A JPH07298868A JP H07298868 A JPH07298868 A JP H07298868A JP 9676394 A JP9676394 A JP 9676394A JP 9676394 A JP9676394 A JP 9676394A JP H07298868 A JPH07298868 A JP H07298868A
Authority
JP
Japan
Prior art keywords
malt
saccharification
whiskey
fermentation
grain
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
JP9676394A
Other languages
Japanese (ja)
Inventor
Isamu Yamada
田 勇 山
Tadao Koyama
山 忠 夫 小
Satoyuki Fukushige
重 智 行 福
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kirin Distillery Co Ltd
Original Assignee
Kirin Distillery Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kirin Distillery Co Ltd filed Critical Kirin Distillery Co Ltd
Priority to JP9676394A priority Critical patent/JPH07298868A/en
Publication of JPH07298868A publication Critical patent/JPH07298868A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide a method for producing grain whisky, designed to impart the flavor stemmed from the fermentation product of malt component through increasing malt proportion along with suppressing the unfavorable flavor derived from grain skin. CONSTITUTION:In this production method for whisky using grain starch material and malt as feedstocks, the fermentative saccharification of the grain starch material and malt is conducted independently of each other. After separating malt lees from the fermentative saccharification liquor from the malt, the resultant liquor is mixed with the fermentative saccharification liquor from the grain starch material and the resultant mixture is fermented, followed by distillation to obtain the objective whisky. By this method, fermentation can be performed with desired design of the flavor stemmed from the fermentation product of malt component and that of grain starch component, enabling preparation and fermentation suppressed in the unfavorable flavor derived from grain skin and thus obtaining the objective whisky with unique flavor and good body.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】〔発明の背景〕BACKGROUND OF THE INVENTION

【産業上の利用分野】本発明は、コーンあるいは米のよ
うな穀類澱粉質材料(この様な穀類澱粉質材料には米麦
系の穀皮は殆ど含まれない)と麦芽により製造されるウ
イスキーの製造方法に関する。本発明製造方法は、麦芽
成分の発酵生成物由来のフレーバーを付与すると共に、
穀類澱粉質材料の発酵生成物由来のフレーバーを付与し
て両フレーバーの調和を可能とし、しかも、穀皮成分由
来の好ましくない香気を抑制したいゆるグレンウイスキ
ーの製造を可能とするものである。
FIELD OF THE INVENTION The present invention relates to a cereal starchy material such as corn or rice (such a cereal starchy material contains almost no barley bark) and malt-produced whiskey. Manufacturing method. The production method of the present invention imparts a flavor derived from a fermentation product of a malt component,
A flavor derived from a fermentation product of a grain starch material is imparted to enable both flavors to be harmonized, and moreover, it is possible to produce a loose grain whiskey in which an undesirable aroma derived from a husk component is suppressed.

【0002】[0002]

【従来の技術】ウイスキーは、使用される原料によって
大きく二つに分けられる。一つは麦芽を原料として糖
化、発酵、蒸留(単式蒸留)されるものであり、モルト
ウイスキーと呼ばれる。もう一つは、コーン(とうもろ
こし)、ライ麦、小麦などの未発芽穀類を蒸煮(または
低温緩蒸煮)後、麦芽を用いて糖化し、発酵、蒸留(通
常連続式蒸留)されるものであり、グレンウイスキーと
呼ばれる。従来、未発芽穀類としてコーン澱粉質粉粒体
のような穀類澱粉質材料を用いるウイスキーの製造のた
めの仕込糖化は、穀類澱粉質材料に酵素剤と麦芽を加え
て、一体の仕込釜で糖化するのが通例である(「醸造の
辞典」、朝倉書店、発行(1988年),第307 〜第312
頁)。穀類澱粉質材料の代表的なものはコーンである
が、このほか小麦、大麦、ライ麦、米穀等が用いられ、
それぞれの穀類成分の発酵由来のフレーバーを付与して
いる。これらの穀類澱粉質材料を仕込糖化するに際し
て、その糖化酵素の供給源として通常麦芽が用いられ
る。麦芽はこの穀類澱粉質材料を糖化する酵素の供給源
だけでなく、麦芽成分発酵生成物由来のフレーバー付与
に貢献している。しかし当該フレーバーの付与のために
麦芽の割合を多くすると麦芽由来の好ましくない香気も
仕込発酵過程で生成する。特開昭60-176579 号公報に
は、穀類澱粉質材料を成形された澱粉生成物とし、糖化
酵素源として麦芽を用いてウイスキー、ジンあるいはウ
オッカを製造する方法が開示されている。この方法で
は、この麦芽を澱粉生成物と一体として仕込糖化液を形
成し、発酵を行っているので、上記のような問題点が依
然として残されている。特開平1-95765 号公報には、ア
スペルギルス・カワチを酵素供給源として、麦芽酵素と
ともに未発芽穀物を仕込糖化する方法が記載されている
が、麦芽は未発芽穀類と一体としてもろみを形成してい
る点では前記のような方法と同じで、麦芽割合を増した
際の問題点等が同様に残されている。なお、特開平1-12
4373号公報には、麦芽の酵素供給源の代わりに発芽米を
用い、米とともに仕込糖化させ発酵、蒸留する方法が記
載されているが、この方法のものは麦芽を使用していな
いので、麦芽成分の発酵生成物由来のフレーバー付与が
できない。
2. Description of the Related Art Whiskey is roughly divided into two types depending on the raw materials used. One is malt whiskey, which is saccharified, fermented, and distilled (single distillation) using malt as a raw material. The other is that corn (corn), rye, wheat and other ungerminated grains are steamed (or slowly steamed), saccharified using malt, fermented and distilled (usually continuous distillation), Called Glen Whiskey. Conventionally, saccharification for the production of whiskey that uses a cereal starchy material such as corn starchy granules as an ungerminated cereal is carried out by adding an enzyme agent and malt to the cereal starchy material and saccharifying it in an integrated charging pot. It is customary to do ("Dictionary of Brewing", Asakura Shoten, published (1988), No. 307-312.
page). Corn is a typical cereal starchy material, but wheat, barley, rye, rice, etc. are also used,
Flavor derived from fermentation of each grain component is added. When charging and saccharifying these cereal starch materials, malt is usually used as the source of the saccharifying enzyme. Malt contributes not only to the source of the enzyme for saccharifying the cereal starch material, but also to the flavor imparted from the fermentation product of the malt component. However, if the proportion of malt is increased to impart the flavor, an unpleasant aroma derived from malt is also generated in the fermentation process. Japanese Unexamined Patent Publication No. 60-176579 discloses a method for producing whiskey, gin or vodka by using a cereal starch material as a shaped starch product and malt as a saccharifying enzyme source. In this method, this malt is integrated with the starch product to form a charged saccharified solution and fermentation is carried out, so that the above-mentioned problems still remain. Japanese Unexamined Patent Publication No. 1-95765 discloses a method in which Aspergillus kawachi is used as an enzyme source to charge and saccharify ungerminated grains together with malt enzyme, but malt forms moromi together with ungerminated grains. The point is that it is the same as the above-mentioned method, and the problems when increasing the malt ratio and the like remain. Incidentally, Japanese Patent Laid-Open No. 1-12
4373 discloses a method of using germinated rice in place of the malt enzyme source, fermenting and saccharification with rice together with distillation, but since malt is not used in this method, malt is used. Flavor derived from the fermentation product of the component cannot be imparted.

【0003】〔発明の概要〕[Outline of Invention]

【発明が解決しようとする課題】本発明は、米、コーン
などの、米麦系の穀皮を除いたあるいは穀皮のない未発
芽の穀類を原料とし、これに麦芽および酵素剤を用いて
糖化された仕込糖化液を発酵させた後、蒸留するウイス
キーの製造法において、麦芽割合を増して、麦芽成分の
発酵生成物由来のフレーバーを付与し、しかも麦芽由来
の好ましくない香気を抑制した、いわゆるグレンウイス
キーの製造技術を提供することを目的とするものであ
る。
DISCLOSURE OF THE INVENTION The present invention uses, as a raw material, ungerminated cereals such as rice and corn, from which rice barley-based hulls have been removed or without hulls, and malt and enzyme agents After fermenting the saccharified charged saccharified liquid, in the method for producing whiskey to be distilled, the malt ratio is increased, a flavor derived from the fermentation product of the malt component is imparted, and undesired aroma derived from malt is suppressed. It is intended to provide a so-called Glen whiskey manufacturing technique.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
の本発明によるウイスキーの製造方法は、穀類澱粉質材
料(米麦系の穀皮のないもしくは除去された穀類および
その加工成型物をさす)と麦芽および糖化酵素源を用い
て製造されるウイスキーの製造方法において、穀類澱粉
質材料の仕込糖化と、麦芽の仕込糖化とを別体で行い、
麦芽の仕込糖化液から麦芽粕を分離後、該麦芽糖化液と
前記穀類澱粉質材料の仕込糖化液とを混合し、その後該
混合液について酵母による発酵を行った後、蒸留するこ
とを特徴とするものである。
A method for producing whiskey according to the present invention for achieving the above object is to describe a cereal starch material (rice or barley-free cereal grains or processed cereals and processed moldings thereof). ) And malt and a method for producing whiskey produced using a saccharifying enzyme source, the saccharification of the cereal starch material and the saccharification of malt are carried out separately.
After separating the malt lees from the malt charge saccharification solution, the malt saccharification solution and the cereal starchy material charge saccharification solution are mixed, after which the mixture is fermented with yeast and then distilled. To do.

【0005】〔発明の具体的説明〕本発明によるウイス
キーの製造方法は、基本的に穀類澱粉質材料の仕込糖化
工程、麦芽の仕込糖化工程、穀類澱粉質材料の糖化液と
麦芽の糖化液(麦芽粕を分離したもの)との混合液につ
いての発酵工程および発酵液についての蒸留工程とから
なるものである。
[Detailed Description of the Invention] The method for producing whiskey according to the present invention basically comprises a step of saccharification of cereal starch material, a step of saccharification of malt, a saccharification solution of cereal starch material and a saccharification solution of malt ( And a distillation step for the fermented liquid.

【0006】穀類澱粉質材料の仕込糖化工程において、
用いる穀類澱粉質材料としては、通常グレンウイスキー
の製造に用いられる穀類澱粉質材料、例えばコーン、大
麦、小麦、ライ麦あるいは米等の穀類から殻皮を除去し
た澱粉質材料が用いられるが、本発明によるウイスキー
の製造方法においては、穀皮を除去したいわゆる米の粉
体もしくは粒体を用いるのが特に好ましい。この工程で
使用される糖化酵素源は、糖化酵素を主体とするもので
あるが、通常グレンウイスキーに使用される酵素源を使
用することができ、特に限定はされない。このような糖
化酵素源としては、アミラーゼを主体とした酵素源、例
えば、麦芽より抽出される酵素剤や、枯草菌等の細菌や
リゾップス属、アスペルギルス属等の糸状菌の生産する
アミラーゼ主体の酵素剤などが、単独もしくは併せて用
いられうる。上記のように糖化酵素源としては、発芽穀
類から抽出されるものに限らず、微生物から抽出される
ものも使用することができる。さらに、必要に応じて穀
皮を除去した粉砕麦芽を補強添加しても良い。また、酵
素力を補強する意味で僅かな量であれば通常の麦芽を加
えても良い。この場合は1〜3%(穀類澱粉質材料に対
して)程度にとどめる。この工程における糖化反応は、
米麦系の穀皮が殆どない(又は極めて少ない)状態であ
ることを除けば、通常のグレンウィスキーの製造におけ
る糖化反応条件に従って行うことができる。
In the saccharification process of the cereal starchy material,
As the cereal starchy material to be used, a cereal starchy material usually used in the production of Glen whiskey, for example, a starchy material obtained by removing the shell of a kernel such as corn, barley, wheat, rye or rice is used. In the method for producing whiskey according to the above, it is particularly preferable to use so-called rice powder or granules from which the husks have been removed. The saccharifying enzyme source used in this step is mainly composed of a saccharifying enzyme, but an enzyme source usually used for Glen whiskey can be used and is not particularly limited. As such a saccharifying enzyme source, an enzyme source mainly composed of amylase, for example, an enzyme agent extracted from malt, an enzyme mainly composed of amylase produced by bacteria such as Bacillus subtilis and filamentous fungi such as Rhizopus and Aspergillus. Agents and the like can be used alone or in combination. As described above, the saccharifying enzyme source is not limited to those extracted from germinated cereals, and those extracted from microorganisms can also be used. Further, crushed malt from which the hulls have been removed may be added as a reinforcement, if necessary. Ordinary malt may be added in a small amount in order to reinforce the enzyme activity. In this case, it is limited to about 1 to 3% (based on the cereal starch material). The saccharification reaction in this step is
It can be carried out according to the saccharification reaction conditions in the usual production of Glen whiskey, except that rice barley-based hulls are almost absent (or extremely absent).

【0007】麦芽の仕込糖化工程において、麦芽はウィ
スキーの製造に通常使用されているものであればよく、
またその使用割合量は特に限定されず、モルトウィスキ
ーの製造において通常使用されている範囲でよい。この
工程における糖化反応は、通常のモルトウィスキーの製
造における糖化反応条件に従って行うことができる。
In the malt preparation saccharification step, the malt may be one normally used in the production of whiskey,
Further, the amount of its use is not particularly limited, and may be in the range usually used in the production of malt whiskey. The saccharification reaction in this step can be carried out according to the saccharification reaction conditions in the usual production of malt whiskey.

【0008】発酵工程、すなわち二種の糖化液の混合液
(穀類澱粉質材料の仕込糖化液および麦芽の仕込糖化液
から麦芽粕を分離した麦汁)についての発酵工程におい
て、発酵反応自体は通常のグレンウィスキーの製造にお
ける発酵処理条件に従って行うことができる。発酵終了
後、発酵液を蒸留する。蒸留はウィスキーの製造に通常
用いられている単式蒸留または連続蒸留法により行うこ
とができる。
In the fermentation process, that is, in the fermentation process for a mixed liquid of two kinds of saccharified liquids (a saccharified liquid of a cereal starchy material and a wort obtained by separating a malt lees from a saccharified liquid of a malt), the fermentation reaction itself is usually It can be performed according to the fermentation processing conditions in the production of Glen Whiskey. After the fermentation is completed, the fermentation broth is distilled. Distillation can be carried out by a single distillation method or a continuous distillation method that is usually used for producing whiskey.

【0009】以下に、本発明方法の好ましい態様を図面
に基づいて詳細に説明する。まず、穀類澱粉質材料の仕
込糖化工程において、図1の仕込釜A(クッカー)に穀
類澱粉質材料、湯および糖化酵素源を加える。穀類澱粉
質材料は、上記したようなものの中から適宜選択すれば
よく、その使用量は特に限定されないが、通常10〜2
0%程度、好ましくは15〜20%程度である(以下、
%表示は特に断りのない限り原料と湯の合計に対する原
料の重量割合を意味する)。酵素源は、上記のように糖
化酵素を主体とするものであり、通常グレンウイスキー
に使用される酵素源を使用することができる。また、上
記したように酵素力を補強する意味で僅かな量であれば
通常の麦芽を加えても良いが、この場合は1〜3%程度
(穀類澱粉質材料に対し)にとどめる。次に、仕込釜内
液を、グレンウイスキーの製造における通常の反応条件
に従って、その穀類澱粉質材料の糊化・膨潤化および糖
化酵素の働く温度を順次経由させて、糖化を達成させ
る。この仕込釜内は、米麦系の穀皮がほとんどないかま
たは極めて少ない状態である。
Hereinafter, preferred embodiments of the method of the present invention will be described in detail with reference to the drawings. First, in the charging saccharification step of the cereal starch material, the cereal starch material, hot water and a saccharifying enzyme source are added to the charging pot A (cooker) of FIG. The cereal starch material may be appropriately selected from those mentioned above, and the amount used is not particularly limited, but usually 10 to 2
It is about 0%, preferably about 15 to 20% (hereinafter,
Unless otherwise specified,% means the weight ratio of the raw material to the total of the raw material and the hot water). The enzyme source is mainly composed of saccharifying enzyme as described above, and the enzyme source usually used for Glen whiskey can be used. Further, as described above, ordinary malt may be added in a small amount in order to reinforce the enzymatic activity, but in this case, it is limited to about 1 to 3% (based on the cereal starch material). Next, the saccharification is achieved by sequentially passing through the gelatinization / swelling of the cereal starchy material and the temperature at which the saccharifying enzyme acts on the liquid in the charging pot according to the normal reaction conditions in the production of Glen whiskey. The inside of the charging pot is in a state where there is little or very little rice-hustle-based hulls.

【0010】一方、麦芽の仕込糖化工程において、穀類
澱粉質材料の糖化工程とは別体に、図1の麦芽糖化釜B
(マッシュタン又はマッシュタブ)に通常用いられる粉
砕麦芽および湯を加え、モルトウイスキーの製造におけ
る通常の糖化反応条件に従って、麦芽の糖化を行う。麦
芽の使用量は特に限定されないが、通常10〜20%程
度である。糖化反応後、この糖化液から麦芽粕を除去す
る。通常、麦芽粕である麦芽の穀皮を濾過層にして麦汁
を得る。
On the other hand, in the malt charging saccharification step, separately from the saccharification step of the cereal starch material, the malt saccharification kettle B shown in FIG.
(Mash ton or mash tub) is added with ground malt and hot water usually used, and malt saccharification is performed according to the normal saccharification reaction conditions in the production of malt whiskey. The amount of malt used is not particularly limited, but is usually about 10 to 20%. After the saccharification reaction, malt meal is removed from this saccharified solution. Usually, wort is obtained by using the bark of malt, which is malt cake, as a filter layer.

【0011】上記のようにして得られた仕込糖化液及び
麦汁液は約65℃程度にし、混合し15〜30分程度保
持する。最終的な穀類澱粉質材料と麦芽との混合割合は
特に限定されないが、通常90:10〜60:40程
度、好ましくは80:20〜70:30である。この混
合液はさらに冷却されて発酵槽に送る(通常の発酵温度
まで冷却後混合される場合もありうる)。該混合液に酵
母が添加され、通常の所定の温度および時間で発酵を行
なう。発酵後この発酵液を蒸留(単式蒸留法または連続
蒸留法)して、ウイスキー蒸留液を得る。
The charged saccharified solution and wort solution obtained as described above are heated to about 65 ° C., mixed and held for about 15 to 30 minutes. The final mixing ratio of the cereal starchy material and malt is not particularly limited, but is usually about 90:10 to 60:40, preferably 80:20 to 70:30. This mixed solution is further cooled and sent to a fermenter (may be mixed after being cooled to a normal fermentation temperature). Yeast is added to the mixed solution, and fermentation is carried out at a usual predetermined temperature and time. After fermentation, the fermentation broth is distilled (single distillation method or continuous distillation method) to obtain a whiskey distillate.

【0012】なお、仕込糖化の際、仕込水の一部に替え
て蒸留残液を用いる通常「サワーマッシュ」と呼ばれる
pHの調整、あるいは乳酸などの添加によるpHの調整
を行うこともできる。上述のような方法により、比較的
高温の穀類澱粉質材料の仕込糖化液から穀皮を殆ど排除
し、しかも発酵前の麦芽粕の分離によって発酵工程で穀
皮の殆ど無い状態にあるため、穀皮成分由来の好ましく
ない香気を抑制して、麦芽の割合を増しても、付与した
い麦芽成分の発酵生成物由来のフレーバーを設計通り付
与することが可能になり、香り高いウイスキーを製造す
ることが可能となった。
During the saccharification of the charge, it is also possible to adjust the pH, which is usually called "sour mash", in which the distillation residual liquid is used instead of a part of the charge water, or the pH is adjusted by adding lactic acid or the like. By the method as described above, almost all the husks are removed from the saccharified liquid of the relatively high temperature cereal starchy material, and moreover, there is almost no husks in the fermentation process due to the separation of the malt meal before fermentation. By suppressing the unpleasant aroma derived from the skin component and increasing the proportion of malt, it becomes possible to impart the flavor derived from the fermentation product of the malt component to be imparted as designed, and it is possible to produce a scented whiskey. It has become possible.

【0013】[0013]

【実施例】以下は、本発明を実施例によって更に具体的
に説明するものであり、これにより本発明は限定される
ものではない。実施例1 粉砕米504g、湯2200mlおよび糖化酵素源(液
化型アミラーゼ:約15,000 JLU/g,JIS K7001-1990)
0.3gを昇温降温可能な容器に入れ、75℃,10分
間保持後、95℃で30分間、蒸煮を行い、65℃まで
冷却した。これとは別に温度制御可能な容器に粉砕麦芽
216g、湯1200mlを加え、約65℃で20分間糖
化を行い、濾過し、ここで麦芽粕分を除き、清澄麦汁を
作り、上記仕込糖化液および麦汁を混合後、約20分間
保持してから30℃まで冷却し、これを発酵槽に移し、
酵母を加え、常法の発酵パターン(30℃、3日間)に
より発酵を行い、蒸留は小型単式蒸留器により行って、
ウィスキーを製造した。実施例1における、米と麦芽の
比率は、重量比で70:30である。そのウィスキーを
当社のパネルにより、官能評価試験* を行った。その結
果は表1に示した。また分析値は表2に示した。穀皮成
分由来の好ましくない香気を感じない、独特の香りとこ
くのあるウイスキーが製造された。また、表2の通り、
主要な香気成分の分析値からもバランスのとれたもので
あった。官能評価試験方法* :パネル(9名)により、
絶対評価法を用いて実施した。評価サンプルはアルコー
ル度数20%として供試した。味と香りの特徴をそれぞ
れに記載してもらい、更に穀皮由来の好ましくない香気
(以下、ハスク臭と呼ぶ)を感じるか否かを判定し、パ
ネル全体数の内ハスク臭の感じるパネル数を示し、有意
差検定を行った。
EXAMPLES The present invention will be described in more detail below by way of examples, which should not be construed as limiting the invention. Example 1 Ground rice 504g, hot water 2200ml and saccharifying enzyme source (liquefied amylase: about 15,000 JLU / g, JIS K7001-1990)
0.3 g was put in a container capable of raising and lowering the temperature, held at 75 ° C. for 10 minutes, steamed at 95 ° C. for 30 minutes, and cooled to 65 ° C. Separately, 216 g of crushed malt and 1200 ml of hot water are added to a temperature-controllable container, saccharification is performed at about 65 ° C. for 20 minutes, and filtration is performed to remove the malt lees and make clear wort. After mixing the wort and wort, hold for about 20 minutes, then cool to 30 ° C., transfer to a fermenter,
Yeast is added, fermentation is performed according to a conventional fermentation pattern (30 ° C., 3 days), and distillation is performed using a small single-distiller,
Manufactured whiskey. The weight ratio of rice to malt in Example 1 was 70:30. The whiskey was subjected to a sensory evaluation test * by our panel. The results are shown in Table 1. The analytical values are shown in Table 2. A whiskey with a unique scent and abundance was produced without feeling the unpleasant aroma derived from the husk component. Also, as shown in Table 2,
It was well balanced from the analysis values of the main fragrance components. Sensory evaluation test method * : By panel (9 people)
It carried out using the absolute evaluation method. The evaluation sample was tested with an alcohol content of 20%. We asked each person to describe the characteristics of taste and scent, and further judged whether or not they felt an unpleasant aroma derived from the husk (hereinafter referred to as "husk odor"). Shown and a significant difference test was performed.

【0014】比較例1 粉砕米504g,湯3200mlおよび糖化酵素源(液
化型アミラーゼ:約15,000 JLU/g,JIS K7001-1990)
0.3gを昇温降温可能な容器に入れ、75℃、10分
間保持後、95℃30分間蒸煮を行い、これを一旦65
℃まで温度を下げ、粉砕麦芽216gを加え15分間保
持した。約30℃まで冷却却後、これを発酵槽に移送
し、酵母を加え、常法の発酵パターン(30℃、3日
間)により発酵を行い、蒸留して、ウィスキーを製造し
た。そのウィスキーを同様に、官能評価試験* を行っ
た。その結果は表1に示した。穀皮成分由来の好ましく
ない香気が感じられ、こくはあるものの香りに問題のあ
るウイスキーであった。
Comparative Example 1 504 g of ground rice, 3200 ml of hot water, and saccharifying enzyme source (liquefied amylase: about 15,000 JLU / g, JIS K7001-1990)
Place 0.3 g in a container that can raise and lower the temperature, hold at 75 ° C for 10 minutes, and boil at 95 ° C for 30 minutes.
The temperature was lowered to ℃, 216 g of ground malt was added, and the mixture was kept for 15 minutes. After cooling to about 30 ° C., this was transferred to a fermenter, yeast was added, fermentation was carried out according to a conventional fermentation pattern (30 ° C., 3 days), and distilled to produce whiskey. The whiskey was similarly subjected to a sensory evaluation test * . The results are shown in Table 1. The whiskey had an unpleasant aroma derived from the husk component and a problem with its aroma although it was rich.

【0015】実施例2 実施例1において、米の仕込糖化では、粉砕米432
g、湯1885mlおよび糖化酵素源(液化型アミラー
ゼ:約15,000 JLU/g,JIS K7001-1990) 0.3gで仕込
糖化を行い、麦芽糖化では、粉砕麦芽288g,湯16
00mlで糖化を行った。その他の条件は実施例1と同
様である。米と麦芽の比率は、60:40である。その
ウィスキーを当社のパネルにより、官能評価試験* を行
った。その結果は表1に示した。穀皮成分由来の好まし
くない香気を感じない、独特の香りとこくのあるウイス
キーであった。
Example 2 In Example 1, in the saccharification of rice, ground rice 432 was used.
g, hot water 1885 ml and saccharifying enzyme source (liquefied amylase: about 15,000 JLU / g, JIS K7001-1990) 0.3 g for saccharification, and malt saccharification, ground malt 288 g, hot water 16
Saccharification was performed with 00 ml. Other conditions are the same as those in the first embodiment. The ratio of rice to malt is 60:40. The whiskey was subjected to a sensory evaluation test * by our panel. The results are shown in Table 1. It was a whiskey with a unique aroma and richness that did not feel the unpleasant aroma derived from the husk component.

【0016】実施例3 実施例1において、米の仕込糖化では、粉砕米576
g,湯2515mlおよび糖化酵素源(液化型アミラー
ゼ:約15,000 JLU/g,JIS K7001-1990) 0. 3gで仕込
糖化を行い、麦芽糖化では、粉砕麦芽144g,湯80
0mlで糖化を行った。その他の条件は実施例1と同様
である。米と麦芽の比率は、80:20である。そのウ
イスキーの官能評価結果は表1に示した。 穀皮成分由
来の好ましくない香気の感じられない独特の香りとこく
のあるウイスキーが製造された。
Example 3 In Example 1, in the saccharification of rice, ground rice 576 was used.
g, 2515 ml of hot water and 0.3 g of saccharifying enzyme source (liquefied amylase: about 15,000 JLU / g, JIS K7001-1990) to perform saccharification, and in malt saccharification, 144 g of ground malt and 80 g of hot water
Saccharification was performed with 0 ml. Other conditions are the same as those in the first embodiment. The ratio of rice to malt is 80:20. The results of sensory evaluation of the whiskey are shown in Table 1. A whiskey with a unique scent and a rich odor that does not have an unpleasant aroma derived from the husk component was produced.

【0017】実施例4 粉砕コーン476g、湯1150ml及び糖化酵素源
(液化型アミラーゼ:約15,000 JLU/g,JIS K7001-199
0) 0.3gを昇温降温可能な容器に入れ、75℃で1
0分間保持後、95℃で30分間蒸煮し、65℃まで冷
却後、粉砕麦芽7gを添加し30分間糖化し、仕込糖化
液を作った。これとは別に温度制御可能な容器に粉砕麦
芽246g及び湯1350mlを加え、実施例1と同様
に清澄麦汁を得た。コーンと麦芽の比率は66:34で
ある。上記仕込糖化液及び麦汁を33℃まで冷却し、こ
れを発酵槽で混合し、酵母を加え33℃で3日間発酵さ
せた。発酵後蒸留を行い、ウイスキーを製造した。その
ウイスキーをパネルにより官能評価試験を行った。結果
を表1に示す。穀皮成分由来の好ましくない香気の殆ど
感じられない、コーン成分の発酵物由来の香りと、麦芽
成分の発酵生成物由来の香りを兼ね備えた独特の香りと
こくのあるウイスキーであった。
Example 4 476 g of crushed corn, 1150 ml of hot water, and saccharifying enzyme source (liquefied amylase: about 15,000 JLU / g, JIS K7001-199)
0) 0.3 g was put in a container capable of raising and lowering the temperature,
After holding for 0 minutes, the mixture was boiled at 95 ° C for 30 minutes, cooled to 65 ° C, added with 7 g of ground malt and saccharified for 30 minutes to prepare a saccharified solution. Separately, 246 g of ground malt and 1350 ml of hot water were added to a temperature-controllable container to obtain clear wort in the same manner as in Example 1. The corn to malt ratio is 66:34. The charged saccharified solution and wort were cooled to 33 ° C, mixed in a fermenter, yeast was added, and fermentation was carried out at 33 ° C for 3 days. Distillation was performed after fermentation to produce whiskey. The whiskey was subjected to a sensory evaluation test using a panel. The results are shown in Table 1. It was a whiskey with a unique scent and a rich scent that combines the scent derived from the fermented product of the corn component and the scent derived from the fermentation product of the malt component in which almost no unpleasant aroma derived from the husk component is felt.

【0018】比較例2 粉砕コーン467g、湯2500ml及び糖化酵素源
(液化型アミラーゼ:約15,000 JLU/g,JIS K7001-199
0) 0.3gを昇温降温可能な容器に入れ75℃で10
分間保持後、95℃で30分間蒸煮し、65℃まで冷却
後、粉砕麦芽253g添加し、30分間糖化し、仕込糖
化液を作った。これを33℃まで冷却し、発酵槽へ移
し、酵母を加え33℃で3日間発酵後、蒸留して、ウイ
スキーを製造した。結果を表1に示した。穀皮成分由来
の好ましくない香気が感じられ、こくはあるものの問題
のあるウイスキーであった。
Comparative Example 2 Grinding corn 467 g, hot water 2500 ml and saccharifying enzyme source (liquefied amylase: about 15,000 JLU / g, JIS K7001-199)
0) 0.3 g was placed in a container capable of raising and lowering the temperature, and 10
After holding for minutes, the mixture was boiled at 95 ° C for 30 minutes, cooled to 65 ° C, added with 253 g of ground malt and saccharified for 30 minutes to prepare a saccharified solution. This was cooled to 33 ° C., transferred to a fermenter, yeast was added thereto, the mixture was fermented at 33 ° C. for 3 days, and then distilled to produce whiskey. The results are shown in Table 1. An unpleasant aroma derived from the husk component was felt, and it was a whiskey with some problems.

【0019】表1 官能評価試験結果 実験例 アルコール 香味比較 ハスク臭を強く 濃度 (%) 特徴 感じるパネル数 香り 味 /全パネル数 実施例1 20% エステリー 雑味なし ** 温和な香気 0/9 比較例1 20% エステリー やや粗さ ** ハスク臭 がある 9/9 青臭い 実施例2 20% エステリー 雑味なし ** 0/9 実施例3 20% エステリー 雑味なし ** 温和な米香気 0/9 実施例4 20% クリーン、 雑味なし ** ハスク臭僅かで、 0/9 気にならない 比較例2 20% ハスク臭、 やや粗さあり ** やや泥臭い 9/9 ** 統計的に有意(危険率1%) Table 1 Results of sensory evaluation test Experimental example Alcohol flavor comparison Strongly husk odor concentration (%) Characteristics Number of panels to be perceived Fragrance Taste / total number of panels Example 1 20% Estery No taste ** Gentle aroma 0/9 Comparison Example 1 20% Esterie Roughness ** Husk odor 9/9 blue odor Example 2 20% Esterie no taste ** 0/9 Example 3 20% Esterie no taste ** Gentle rice aroma 0/9 Example 4 20% clean, no unpleasant taste ** Husk odor, 0/9 Not disturbing Comparative Example 2 20% Husk odor, slightly rough ** Slightly mud odor 9/9 ** Statistically significant (dangerous) 1%)

【0020】表2 分析値(mg/l) 項目 酢酸 酢酸イソ n-プロパ i-ブタ i-アミル エチル アミル ノール ノール アルコール 実験例 ppm ppm ppm ppm ppm 実施例1 31.2 0.4 62.0 285.6 552.8 [0020] Table 2 Analytical values (mg / l) Item acetate acetate isobutyrate n- prop i- pig i- amyl ethyl amyl Nord Nord alcohol Experiment ppm ppm ppm ppm ppm Example 1 31.2 0.4 62.0 285.6 552.8

【0021】[0021]

【発明の効果】本発明によれば、穀類澱粉質材料の糖化
と麦芽の糖化を別体で行わせるため、麦芽成分の発酵生
成物由来のフレーバーと穀類澱粉質成分の発酵生成物由
来のフレーバーを任意に設計した仕込発酵を行うことが
でき、殻皮成分由来の好ましくない香気の抑制された仕
込および発酵をさせることができ、独特の香りとこくの
あるウイスキーを得ることができる。
According to the present invention, in order to perform saccharification of a cereal starch material and saccharification of malt separately, a flavor derived from a fermentation product of a malt component and a flavor derived from a fermentation product of a cereal starch component. It is possible to carry out the fermenting and fermenting which are arbitrarily designed, to control the fermenting and fermenting the undesired aroma derived from the husk component, and to obtain whiskey having a unique aroma and body.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明製造方法のフローチャートを示す説明
図。
FIG. 1 is an explanatory view showing a flowchart of a manufacturing method of the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】穀類澱粉質材料および麦芽を原料にして製
造されるウイスキーの製造方法において、穀類澱粉質材
料の仕込糖化と、麦芽の仕込糖化とを別体で行い、麦芽
の仕込糖化液から麦芽粕を分離後、該麦芽糖化液と前記
穀類澱粉質材料の仕込糖化液とを混合し、その後該混合
液を発酵させて蒸留することを特徴とする、ウイスキー
の製造方法。
1. A method for producing whiskey produced from a cereal starch material and malt as raw materials, wherein the saccharification of the cereal starch material and the saccharification of malt are carried out separately, and a saccharified solution of malt is prepared. A method for producing whiskey, characterized in that after the malt cake is separated, the malt saccharified solution and the charged saccharified solution of the cereal starchy material are mixed, and then the mixed solution is fermented and distilled.
【請求項2】穀類澱粉質材料が米である、請求項1に記
載の方法。
2. The method according to claim 1, wherein the cereal starchy material is rice.
JP9676394A 1994-05-10 1994-05-10 Production of whisky Pending JPH07298868A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9676394A JPH07298868A (en) 1994-05-10 1994-05-10 Production of whisky

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9676394A JPH07298868A (en) 1994-05-10 1994-05-10 Production of whisky

Publications (1)

Publication Number Publication Date
JPH07298868A true JPH07298868A (en) 1995-11-14

Family

ID=14173682

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9676394A Pending JPH07298868A (en) 1994-05-10 1994-05-10 Production of whisky

Country Status (1)

Country Link
JP (1) JPH07298868A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003164265A (en) * 2001-12-03 2003-06-10 Gun Ei Chem Ind Co Ltd Production method of fermented food
KR100882534B1 (en) * 2007-06-15 2009-02-09 농업회사법인 주식회사 부민국제퍼먼텍 How to make an attribute of whiskey or brandy
WO2018207250A1 (en) 2017-05-09 2018-11-15 サントリーホールディングス株式会社 Saccharified liquid, method for producing saccharified liquid, food and beverage, distilled liquid for whiskey, and whiskey
JP2021045164A (en) * 2020-12-15 2021-03-25 サントリーホールディングス株式会社 Saccharification solution, manufacturing method of saccharification solution, food and drink, distillate for whiskey and whiskey

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003164265A (en) * 2001-12-03 2003-06-10 Gun Ei Chem Ind Co Ltd Production method of fermented food
KR100882534B1 (en) * 2007-06-15 2009-02-09 농업회사법인 주식회사 부민국제퍼먼텍 How to make an attribute of whiskey or brandy
WO2018207250A1 (en) 2017-05-09 2018-11-15 サントリーホールディングス株式会社 Saccharified liquid, method for producing saccharified liquid, food and beverage, distilled liquid for whiskey, and whiskey
KR20190138678A (en) 2017-05-09 2019-12-13 산토리 홀딩스 가부시키가이샤 Saccharified liquid, manufacturing method of saccharified liquid, food and drink, distilled liquid for whiskey and whiskey
CN110603314A (en) * 2017-05-09 2019-12-20 三得利控股株式会社 Saccharified solution, method for producing saccharified solution, food and drink, distillate for whisky, and whisky
JPWO2018207250A1 (en) * 2017-05-09 2020-01-16 サントリーホールディングス株式会社 Saccharified solution, saccharified solution manufacturing method, food and drink, whiskey distillate, and whiskey
AU2017413867B2 (en) * 2017-05-09 2020-07-30 Suntory Holdings Limited Saccharified liquid, method for producing saccharified liquid, food and beverage, distilled liquid for whiskey, and whiskey
EP3623460A4 (en) * 2017-05-09 2020-12-16 Suntory Holdings Limited SUGARED LIQUID, PROCESS FOR MANUFACTURING SUGARCED LIQUID, FOOD AND BEVERAGE, DISTILLED LIQUID FOR WHISKEY AND WHISKEY
KR20220093258A (en) 2017-05-09 2022-07-05 산토리 홀딩스 가부시키가이샤 Saccharified liquid, method for producing saccharified liquid, food and beverage, distilled liquid for whiskey, and whiskey
JP2021045164A (en) * 2020-12-15 2021-03-25 サントリーホールディングス株式会社 Saccharification solution, manufacturing method of saccharification solution, food and drink, distillate for whiskey and whiskey

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