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JP3432599B2 - Production method of fermented malt beverage - Google Patents
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JP3432599B2 - Production method of fermented malt beverage - Google Patents

Production method of fermented malt beverage

Info

Publication number
JP3432599B2
JP3432599B2 JP15173994A JP15173994A JP3432599B2 JP 3432599 B2 JP3432599 B2 JP 3432599B2 JP 15173994 A JP15173994 A JP 15173994A JP 15173994 A JP15173994 A JP 15173994A JP 3432599 B2 JP3432599 B2 JP 3432599B2
Authority
JP
Japan
Prior art keywords
beer
fermented
wort
malt beverage
temperature
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 - Fee Related
Application number
JP15173994A
Other languages
Japanese (ja)
Other versions
JPH07327656A (en
Inventor
達二 森本
彰 横野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sapporo Breweries Ltd
Sapporo Holdings Ltd
Original Assignee
Sapporo Breweries Ltd
Sapporo Holdings Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sapporo Breweries Ltd, Sapporo Holdings Ltd filed Critical Sapporo Breweries Ltd
Priority to JP15173994A priority Critical patent/JP3432599B2/en
Publication of JPH07327656A publication Critical patent/JPH07327656A/en
Application granted granted Critical
Publication of JP3432599B2 publication Critical patent/JP3432599B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、発酵麦芽飲料の製造法
に関する。発酵麦芽飲料は主にビールを意味し、低アル
コール濃度のビール等も包含される。
TECHNICAL FIELD The present invention relates to a method for producing a fermented malt beverage. The fermented malt beverage mainly means beer, and also includes beer having a low alcohol concentration.

【0002】[0002]

【従来の技術】ビール等の発酵麦芽飲料(以下「ビー
ル」として説明する)の製造方法の歴史は非常に古く、
技術的にはすでに確立されているといってよい。すなわ
ち、基本的なビール製造技術は以下の工程より構成され
ている。 1.仕込工程 仕込槽にて麦芽に温水を加えて(場合によっては米等の
副原料を添加する)マイシェ(粥状のもの)を造り、麦
芽のでんぷん質を麦芽糖を主体とする糖に変え、蛋白質
を可溶化させる。 2.濾過工程(麦汁濾過) 上記マイシェを濾過して糖液(以下「麦汁」と称する)
を得る。 3.煮沸工程 上記麦汁を煮沸釜で煮沸する。この時ホップも添加さ
れ、苦味が形成され蛋白質の凝固が行われる。 4.発酵工程 上記麦汁を6〜8℃に冷却した後、酵母を添加して、主
発酵(一次発酵:麦汁を5〜10℃で7〜8日間発酵さ
せ、発酵麦汁(以下「若ビール」という)を造る)を行
う。次に、この若ビールを貯酒タンクに移し、後発酵
(二次発酵:若ビールを0〜1℃の低温で約1カ月程度
熟成させる。)させる。なお、アルコール濃度と炭酸ガ
ス含有量は一次発酵の工程でほぼ決まる。 5.濾過工程(二次濾過) 後発酵を終了し、清澄になったビールをさらに、最終的
に濾過する。 以上のように、ビール等の発酵麦芽飲料は基本的に上記
の伝統的な工程を経て製造される。
2. Description of the Related Art The history of the manufacturing method of fermented malt beverages such as beer (hereinafter referred to as "beer") is very old,
It is technically already established. That is, the basic beer manufacturing technology is composed of the following steps. 1. Preparation process In the preparation tank, warm water is added to malt (additional raw materials such as rice are added in some cases) to make a maiche (porridge-like), and the malt starch is converted to maltose-based sugar and protein is added. Is solubilized. 2. Filtration Step (Wort Filtration) A sugar solution (hereinafter referred to as "wort") by filtering the above-mentioned maichet
To get 3. Boiling step The above wort is boiled in a boiling pot. At this time, hops are also added, bitterness is formed, and protein is coagulated. 4. Fermentation step After cooling the wort to 6 to 8 ° C, yeast is added to perform main fermentation (primary fermentation: wort is fermented at 5 to 10 ° C for 7 to 8 days, and fermented wort (hereinafter referred to as “young beer )) Is made). Next, the young beer is transferred to a storage tank and post-fermented (secondary fermentation: the young beer is aged at a low temperature of 0 to 1 ° C. for about 1 month). The alcohol concentration and the carbon dioxide content are almost determined by the primary fermentation process. 5. Filtration Step (Secondary Filtration) After the fermentation is completed, the clarified beer is finally filtered. As described above, fermented malt beverages such as beer are basically manufactured through the above-mentioned traditional process.

【0003】しかしながら、こうして造られたビールは
温度等の環境変化により、飽和状態を越えて凝固・析出
成分および平衡状態の崩れで構造の変化を来し、凝
固・析出す成分を含むため、いわゆる混濁を来しやす
い。特に、ビールは一般的に冷やして飲まれる場合が多
く、寒冷混濁、凍結混濁が問題になるケースが多い。こ
れらの混濁はビール中の成分の一部(寒冷混濁の場合:
蛋白質やポリフェノール、凍結混濁の場合:主にβ−グ
ルカンなどの炭水化物が主体)が低温下で凝固・析出す
る。これらは室温に戻すことにより消失する場合もある
が、これによって味も変化し、商品価値を失うこととな
る。
However, thus produced beer by environmental changes such as temperature, Kitashi changes in structure collapse ingredients and equilibrium you coagulation and precipitation <br/> over the saturated state, to coagulation and precipitation Since it contains the components, so-called turbidity is likely to occur. In particular, beer is often chilled for drinking, and cold turbidity and freeze turbidity often cause problems. These turbidities are part of the ingredients in beer (in the case of cold turbidity:
In the case of proteins, polyphenols, and freeze turbidity: mainly carbohydrates such as β-glucan) coagulate and precipitate at low temperatures. These may disappear by returning to room temperature, but this changes the taste and loses commercial value.

【0004】この問題を解決するために、例えば低温で
長期間貯蔵して混濁の原因となる成分を析出・沈殿させ
る方法が考えられる。また、その他の方法として、熟成
を終えたビールを凍結温度まで下げ、凍結させてシャー
ベット状態として所定時間寝かせ、氷中に混濁成分を凝
固・析出させた後、ビールシャーベットから氷(一部ま
たは全部)を分離、除去して混濁成分をビール中より排
除する方法も可能性として考えられる(以下「凍結法」
と称する)。
In order to solve this problem, for example, a method of storing at low temperature for a long period of time to precipitate / precipitate a component causing turbidity can be considered. In addition, as another method, the beer after aging is lowered to a freezing temperature, frozen and allowed to stand in a sherbet state for a predetermined time, and the cloudy components are coagulated / precipitated in the ice, and then the beer sherbet is cooled (partly or entirely). ) May be separated and removed to remove turbid components from the beer (hereinafter referred to as "freezing method").
Called)).

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記低
温長期貯蔵の方法は製造時間が大幅に増加し、製造効率
が大幅に悪化することは目に見えている。一方、上記凍
結法では、混濁成分以外のビールエキス分等排除する必
要のない成分まで氷中に吸収・析出させてしまう可能性
があり、本質的にビールの味を損なう危険性がある。し
かも、多くの水分が失われてしまうため、相対的にアル
コール濃度が高くなり、これも味の変化を招来する原因
となる。さらに、シャーベット状態であるため、ビール
の流動性が著しく低下することとなり、製造に時間を要
し、製造効率が悪化する。
However, it is apparent that the above-mentioned low temperature long-term storage method significantly increases the manufacturing time and significantly deteriorates the manufacturing efficiency. On the other hand, in the above-mentioned freezing method, there is a possibility that components such as beer extract other than the turbid component that do not need to be removed may be absorbed and deposited in ice, and there is a risk of essentially impairing the taste of beer. Moreover, since much water is lost, the alcohol concentration is relatively high, which also causes a change in taste. Further, since it is in the sherbet state, the fluidity of beer is significantly reduced, which requires time for production and deteriorates production efficiency.

【0006】本発明は上述した技術的問題点を解決する
ことを目的とするものであり、製造効率を悪化させるこ
となく、あらかじめ混濁を発生させる成分を析出・排除
することにより、混濁の発生しない、すなわち混濁耐久
性のある発酵麦芽飲料の製造法を提供することにある。
さらに、発酵麦芽飲料の本質的な味や特性を損なうこと
なく、雑味のない、すっきりとした切れのある発酵麦芽
飲料の製造法を提供するものである。
The present invention is intended to solve the above-mentioned technical problems, and does not cause turbidity by preliminarily depositing and eliminating components that cause turbidity without deteriorating the production efficiency. That is, it is to provide a method for producing a fermented malt beverage having cloudiness durability.
Further, the present invention provides a method for producing a fermented malt beverage which is clean and has no unpleasant taste, without impairing the essential taste and characteristics of the fermented malt beverage.

【0007】[0007]

【課題を解決するための手段】すなわち、本発明は請求
項1に記載したように、発酵麦芽飲料の製造法におい
て、麦汁を一次発酵工程にて発酵させることにより得ら
れた発酵麦汁を凍結温度付近の温度範囲である−1.0
〜−4.0℃まで1日〜10日を費やして緩慢に冷却
し、該冷却発酵麦汁を過冷却状態にて流動させながら二
次発酵工程に供給し、発酵させることを特徴とする発酵
麦芽飲料の製造法を提供すると共に、請求項2に記載し
たように、発酵麦芽飲料の製造法において、麦汁を一次
発酵工程にて発酵させることにより得られた発酵麦汁を
凍結温度付近の温度範囲である−1.0〜−4.0℃ま
1日〜10日を費やして緩慢に冷却し、該冷却発酵麦
汁を過冷却状態にて流動させた後、該過冷却状態の発酵
麦汁を濾過工程を経て二次発酵工程に供給し、新たに醸
造用酵母を添加して二次発酵を行うことを特徴とする発
酵麦芽飲料の製造法を提供するものである。
That is, according to the present invention, as described in claim 1, in a method for producing a fermented malt beverage, a fermented wort obtained by fermenting wort in a primary fermentation step is used. It is the temperature range near freezing temperature -1.0
Fermentation characterized by slowly cooling to −4.0 ° C. for 1 to 10 days , supplying the secondary fermentation step while flowing the cooled fermented wort in a supercooled state, and fermenting While providing a method for producing a malt beverage, as described in claim 2, in the method for producing a fermented malt beverage, the fermented wort obtained by fermenting wort in the primary fermentation step has a temperature around freezing temperature. After slowly cooling to a temperature range of -1.0 to -4.0 ° C for 1 to 10 days , the cooled fermented wort was allowed to flow in a supercooled state, and The fermented wort in a supercooled state is supplied to a secondary fermentation step through a filtration step, and a method for producing a fermented malt beverage characterized by performing secondary fermentation by newly adding brewing yeast is provided. is there.

【0008】本発明の発酵麦芽飲料の製造法は、請求項
1に示す如く、一次発酵を終えた麦汁(若ビール)を凍
結温度付近の温度範囲である−1.0〜−4.0℃まで
1日〜10日を費やして緩慢に冷却し、この冷却発酵麦
汁をさらに過冷却状態にて所定時間流動させた後、二次
発酵工程(「貯酒工程」とも言う)に供給する方法であ
る。また、請求項2に示す発酵麦芽飲料の製造法では、
上記冷却発酵麦汁を過冷却状態で所定時間流動させた
後、濾過工程を経て二次発酵工程に供給し、新たに醸造
用酵母を添加して二次発酵を行わせる。いずれの方法に
おいても、二次発酵終了後、濾過を行って製品化され
る。
In the method for producing a fermented malt beverage according to the present invention, as described in claim 1, the wort (young beer) that has undergone the primary fermentation is in the temperature range near the freezing temperature of -1.0 to -4.0. Up to ℃
It is a method of slowly cooling it by spending 1 to 10 days, allowing this cooled fermented wort to further flow in a supercooled state for a predetermined time, and then supplying it to a secondary fermentation step (also referred to as a "storing step"). . Further, in the method for producing a fermented malt beverage according to claim 2,
After the cooled fermented wort is allowed to flow in a supercooled state for a predetermined time, it is supplied to the secondary fermentation step through a filtration step, and brewing yeast is newly added to carry out secondary fermentation. In either method, after the secondary fermentation is completed, filtration is performed to obtain a product.

【0009】[0009]

【作用】本発明は、請求項1如く構成することによっ
て、混濁を引き起こすビール中の成分を凝固・析出させ
ると共にビール中に含まれる雑味成分も併せて凝固・析
出する。また、請求項2の方法では、二次発酵貯工程前
に、析出した混濁成分および雑味成分を濾過し、このと
き酵母も濾過されてしまうため、二次発酵工程時に新た
に醸造用酵母を添加して二次発酵を行う。
According to the present invention, by constructing as described in claim 1, the components in beer that cause turbidity are coagulated / precipitated, and the miscellaneous components contained in beer are also coagulated / precipitated. Further, in the method of claim 2, before the secondary fermentation storage step, the precipitated cloudy components and miscellaneous components are filtered, and the yeast is also filtered at this time, so that a new brewing yeast is added during the secondary fermentation step. Add and perform secondary fermentation.

【0010】[0010]

【実施例】次に、本発明の実施例を図面に基づいて説明
する。 実施例1 図1は、本発明の実施例を示すビールの製造工程図であ
り、図2は、図1の製造工程における冷却槽の一実施態
様を示す。なお、本実施例のビール製造法は、仕込工程
から一次発酵工程まで、前記従来のビール製造方法と基
本的に変わりないので、これら工程についての詳細な説
明は省略する。さて、図1において、1は一次発酵タン
クであり、これは発酵タンク2と該タンク2の周囲を覆
う冷却用ジャケット3より構成されている。冷却用ジャ
ケットには図示されていない冷却器より冷媒が供給さ
れ、発酵タンク2内を冷却するものである。なお、冷却
器としては、一般的なヒートポンプ方式を使用している
が、冷媒を用いない、ペルチエ素子を使用した電子冷却
方式を用いてもよい。
Embodiments of the present invention will now be described with reference to the drawings. Example 1 FIG. 1 is a process drawing of beer showing an example of the present invention, and FIG. 2 shows one embodiment of a cooling tank in the manufacturing process of FIG. Since the beer production method of this example is basically the same as the conventional beer production method from the charging step to the primary fermentation step, detailed description of these steps will be omitted. Now, in FIG. 1, reference numeral 1 is a primary fermentation tank, which is composed of a fermentation tank 2 and a cooling jacket 3 covering the periphery of the tank 2. Refrigerant is supplied from a cooler (not shown) to the cooling jacket to cool the fermentation tank 2. As the cooler, a general heat pump system is used, but an electronic cooling system using a Peltier element without using a refrigerant may be used.

【0011】次に、4は冷却装置であり、冷却槽5と冷
媒流通槽6から構成されている冷却装置4の具体例は図
2に示されている。一次発酵タンクからの若ビールは冷
却槽5の一端に設けられた注入口7より冷却槽内に供給
し、冷却槽5の他端に設けられた注出口8より排出され
る。また、冷媒流通槽6の一端には冷媒注入口9を備
え、他端には冷媒注出口10を備え、図示しない冷却器
より冷媒が供給される。図中の11は二次発酵タンク
で、従来のビール製造に用いられるものと変わりない。
12は濾過装置であり、これも従来のビール製造におけ
る二次濾過装置と機能・構造とも変わりない。
Next, 4 is a cooling device, and a concrete example of the cooling device 4 comprising a cooling tank 5 and a refrigerant circulation tank 6 is shown in FIG. Young beer from the primary fermentation tank is supplied into the cooling tank through an inlet 7 provided at one end of the cooling tank 5, and is discharged through a pouring port 8 provided at the other end of the cooling tank 5. A coolant inlet 9 is provided at one end of the coolant circulation tank 6, and a coolant outlet 10 is provided at the other end, so that the coolant is supplied from a cooler (not shown). Reference numeral 11 in the figure denotes a secondary fermentation tank, which is the same as that used in conventional beer production.
Reference numeral 12 is a filtration device, which has the same function and structure as the conventional secondary filtration device in beer production.

【0012】ビール製造工程の構成は上記のごとくであ
り、以下この工程図に沿って製造法の詳細を説明する。
麦汁は、温度6〜8℃の環境下、一次発酵タンクに約1
週間程度保持され、いわゆる主発酵が行われる。一次発
酵終了後、冷却ジャケット3に冷媒が供給され、発酵タ
ンク内の若ビールの冷却を開始する。ここで若ビール
は、冷却器の能力、一次発酵タンクの大きさあるいは冷
却する若ビールの量等でも異なるが、ほぼ1日〜10日
費やして、凍結温度付近(ビールの種類によって異な
るが、ビールの凍結温度はほぼ−2.0〜−3.0℃で
ある)の温度範囲(該凍結温度±1℃程度)、すなわち
−1.0〜−4.0℃になるようにゆっくり冷却する。
The structure of the beer manufacturing process is as described above, and the manufacturing method will be described in detail below with reference to the process chart.
About 1 wort is stored in the primary fermentation tank under the environment of temperature 6 ~ 8 ℃.
It is maintained for about a week and so-called main fermentation is performed. After the completion of the primary fermentation, the cooling jacket 3 is supplied with a refrigerant to start cooling the young beer in the fermentation tank. Here, the young beer varies depending on the capacity of the cooler, the size of the primary fermentation tank, the amount of the young beer to be cooled, etc., but it is about 1 to 10 days.
And the freezing temperature is around (the freezing temperature of beer is about −2.0 to −3.0 ° C. although it varies depending on the type of beer) (the freezing temperature is about ± 1 ° C.), that is, −1. Slowly cool to 0 to -4.0 ° C.

【0013】一次発酵タンク内で静止するビールを上記
温度範囲内に調整し、かつビール全体を凍結させない様
にするには、例えば直接液温を監視し、そのデータに基
づいて冷媒の流量、冷媒の温度等を制御したり、冷媒の
温度を監視し、そのデータに基づいて冷媒の流量、温度
等を制御して厳密な温度管理をする必要がある。次に、
凍結温度付近まで冷却された若ビールを発酵タンクより
取り出し、冷却装置4の冷却槽5内に導入し、槽5内を
注入口7より注出口8に向かって流通させつつ−2.5
〜−3.0℃に冷却し、若ビールを過冷却状態とする。
この状態における若ビールは、わずかに氷結晶が形成さ
れるものの凍結はしておらず、充分に流動性を持ってい
る。
In order to regulate the beer stationary in the primary fermentation tank within the above temperature range and prevent the entire beer from freezing, for example, the liquid temperature is directly monitored, and the flow rate of the refrigerant and the refrigerant are determined based on the data. It is necessary to strictly control the temperature and the like or to monitor the temperature of the refrigerant and to control the flow rate and the temperature of the refrigerant based on the data to strictly control the temperature. next,
The young beer cooled to around the freezing temperature is taken out from the fermentation tank, introduced into the cooling tank 5 of the cooling device 4, and is circulated in the tank 5 from the injection port 7 toward the spout 8 at −2.5.
Cool to ~ -3.0 ° C to bring the young beer into a supercooled state.
The young beer in this state has a sufficient fluidity, although it does not freeze although ice crystals are slightly formed.

【0014】ビールの過冷却状態を維持するためには、
主に流量の調節がポイントになる。すなわち、流量を制
御することにより若ビールを凍結させることなく過冷却
状態を保つことができる。流量の制御については、あら
かじめ適正な流量を求めておき、これを制御目標値とし
て冷却槽5内の若ビール流量を監視し、検出値と前記目
標値とを比較して得られた誤差に基づいて流量の補正を
行うフィードバック制御を用いても良いし、アイス・セ
ンサーによる若ビール中の氷結晶の増減を検出して目標
値と検出値との誤差に基づいて流量あるいは温度制御を
行う方法、または流通する若ビールの温度を直接監視
し、そのデータに基づいて温度コントロールを行う方法
がある。
In order to maintain the supercooled state of beer,
The main point is to control the flow rate. That is, by controlling the flow rate, the supercooled state can be maintained without freezing the young beer. Regarding the control of the flow rate, an appropriate flow rate is obtained in advance, the flow rate of young beer in the cooling tank 5 is monitored using this as a control target value, and based on the error obtained by comparing the detected value with the target value. Feedback control to correct the flow rate may be used, or a method of detecting the increase / decrease of ice crystals in young beer by an ice sensor and controlling the flow rate or temperature based on the error between the target value and the detected value, Alternatively, there is a method of directly monitoring the temperature of the young beer in circulation and controlling the temperature based on the data.

【0015】なお、上記適正な流量については、冷却槽
5の大きさ、形状等に関係するものであるが、図2に示
す円筒形状の場合、全長1〜10m,内径0.2〜1.
5mの大きさで、約5〜50kl/h( 時間) 程度が適当で
ある。若ビールは過冷却状態で冷却5内を冷却されつつ
流通することにより、液中に含まれる混濁成分および雑
味成分が液中に凝固・析出することとなる。冷却装置4
を流通した若ビールは、次に二次発酵を行うため、二次
発酵タンク11に供給される。なお、冷却装置4を出た
若ビール中には混濁成分が析出しており、このまま二次
発酵タンク11で二次発酵を行うと、液温によっては析
出した混濁成分等が再溶解する可能性が考えられるが、
二次発酵工程を0〜−1℃程度の温度で行うことによ
り、発酵に支障を来すことなく、混濁成分等の再溶解を
防止することができる。
The proper flow rate depends on the size and shape of the cooling tank 5, but in the case of the cylindrical shape shown in FIG. 2, the total length is 1 to 10 m and the inner diameter is 0.2 to 1.
The size of 5 m is suitable for about 5 to 50 kl / h (hour). When the young beer flows while being cooled in the cooling 5 in a supercooled state, the turbid component and the miscellaneous component contained in the liquid are solidified and precipitated in the liquid. Cooling device 4
The young beer that has been distributed in the above step is supplied to the secondary fermentation tank 11 for secondary fermentation. It should be noted that cloudy components are precipitated in the young beer exiting the cooling device 4, and if secondary fermentation is carried out in the secondary fermentation tank 11 as it is, the cloudy components deposited may be redissolved depending on the liquid temperature. Is possible,
By performing the secondary fermentation step at a temperature of about 0 to -1 ° C, it is possible to prevent redissolution of turbid components and the like without affecting the fermentation.

【0016】二次発酵の期間は従来のビールと同等の2
0日〜30日で良い。二次発酵を終了したビールは濾過
器12に供給され、析出された混濁成分、酵母および不
純物等を除去されてビールとなる。本実施例では、上述
した麦汁の冷却を一次発酵タンクにて行ったが、これに
限ることなく、別途冷却設備を設けてもよい。また、二
次発酵工程で混濁成分の再溶解が心配な場合には、二次
発酵工程前に濾過工程を設け、析出した混濁成分等を分
離・排除する。ただしこの場合、酵母も濾過してしまう
ため、二次発酵工程で新たに酵母を添加する必要があ
る。
The period of secondary fermentation is the same as that of conventional beer.
It can be 0 to 30 days. The beer that has undergone the secondary fermentation is supplied to the filter 12, and the precipitated cloudy components, yeast, impurities and the like are removed to become beer. In this example, the cooling of wort described above was performed in the primary fermentation tank, but the present invention is not limited to this, and a separate cooling facility may be provided. Further, when there is a concern that the cloudy components will be redissolved in the secondary fermentation process, a filtration process is provided before the secondary fermentation process to separate and remove the precipitated cloudy components. However, in this case, since yeast is also filtered, it is necessary to newly add yeast in the secondary fermentation step.

【0017】混濁耐久性測定試験 上記の処理を行って得られたビールの混濁耐久性につい
て試験を行った結果を以下に示す。測定は、製造された
ビールを瓶(あるいは缶)に詰め、これをサンプルとし
て60±1℃の恒温水中に立位で72時間浸漬してから
水冷し、次に0℃の氷浴中(Cooling Bat
h)に24時間浸漬し、次いで濁度計のセルに移して0
℃で濁度を測定することにより行った。従来の方法で製
造したビール(従来ビール)と上記方法により製造した
ビール(本発明ビール)とをそれぞれサンプルとして濁
度を測定した結果を以下に示す(単位:EBC単位)。 従来ビール :1.5〜1.6 本発明ビール:0.7〜1.0 濁度測定結果から明らかなように、従来ビールに対して
本発明ビールの濁度は明らかに改善されている。
Turbidity Durability Measurement Test The results of the turbidity durability test of beer obtained by the above treatment are shown below. For the measurement, the beer produced was packed in a bottle (or a can), and this was used as a sample, soaked in constant temperature water at 60 ± 1 ° C for 72 hours in the standing position, then water-cooled, and then in an ice bath at 0 ° C (Cooling). Bat
h) for 24 hours, then transfer to the turbidimeter cell for 0
This was done by measuring turbidity at ° C. The results of measuring the turbidity of beer produced by the conventional method (conventional beer) and beer produced by the above method (the beer of the present invention) as samples are shown below (unit: EBC unit). Conventional beer: 1.5 to 1.6 Beer of the present invention: 0.7 to 1.0 As is clear from the turbidity measurement results, the turbidity of the beer of the present invention is clearly improved with respect to the conventional beer.

【0018】官能試験 次に、本発明ビールと従来ビールとをパネル数10名
で、味に関する官能試験を行った。以下にその結果を示
す。
Sensory Test Next, the beer of the present invention and the conventional beer were subjected to a sensory test concerning taste by 10 panelists. The results are shown below.

【0019】[0019]

【表1】 味項目 本発明ビール 従来ビール 酸味 1 0 甘味 1 0 金属味 0 0 収斂味 0 0 渋味 1 3 雑味 0 3 平板 1 2 老化味 0 0 味コメント数合計 4 8[Table 1]       Taste item Invention beer Conventional beer         Sourness 10         Sweetness 10         Metallic taste 0 0         Astringency 0 0         Astringency 13         Miscellaneous 0 3         Flat plate 1 2         Aging taste 0 0   Total number of taste comments 4 8

【0020】以上の如く、本発明ビールでは明らかにコ
メント数が少なく、特に渋味、雑味の項目は明確に高く
評価されいてることが明らかである。
As described above, it is clear that the beer of the present invention has a small number of comments, and that the items of astringency and sourness are clearly highly evaluated.

【0021】[0021]

【発明の効果】本発明によれば、ビール等の発酵麦芽飲
料の製造過程で生ずる寒冷混濁および凍結混濁を発生さ
せる成分を、製造効率を低下させることなく、析出・排
除することができ、混濁耐久性が大幅に向上する。しか
も、発酵麦芽飲料のエキス濃度,アルコール濃度等発酵
麦芽飲料の基本的成分はほとんど変化させることなく、
雑味を低減することができるので、本来の味を維持しな
がら、すっきりとした切れのある特性が付与される。
EFFECTS OF THE INVENTION According to the present invention, components that cause cold turbidity and freeze turbidity that occur during the production of fermented malt beverages such as beer can be precipitated and eliminated without lowering production efficiency. Durability is greatly improved. Moreover, the basic components of the fermented malt beverage such as the extract concentration and the alcohol concentration of the fermented malt beverage are almost unchanged,
Since the unpleasant taste can be reduced, a clean and sharp characteristic is imparted while maintaining the original taste.

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

【図1】 本発明の1実施例を示すビールの製造工程図
である。
FIG. 1 is a process drawing of beer showing one embodiment of the present invention.

【図2】 図1に示された冷却装置の一部切欠説明図で
ある。
FIG. 2 is a partially cutaway explanatory view of the cooling device shown in FIG.

【符号の説明】[Explanation of symbols]

1 一次発酵タンク 2 発酵タンク 3 冷却ジャケット 4 冷却装置 5 冷却槽 6 冷媒流通槽 11 二次発酵タンク 12 濾過器 1 Primary fermentation tank 2 fermentation tanks 3 cooling jacket 4 Cooling device 5 cooling tanks 6 Refrigerant distribution tank 11 Secondary fermentation tank 12 Filter

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C12C 1/00 - 13/10 C12H 1/00 - 1/22 C12G 3/02 JICST(JOIS) WPI/FOODLINE/FSTA/F OOD ADLIBRA(DIALO G)─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields surveyed (Int.Cl. 7 , DB name) C12C 1/00-13/10 C12H 1/00-1/22 C12G 3/02 JISST (JOIS) WPI / FOODLINE / FSTA / FOOD ADLIBRA (DIALOG)

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 発酵麦芽飲料の製造法において、麦汁を
一次発酵工程にて発酵させることにより得られた発酵麦
汁を凍結温度付近の温度範囲である−1.0〜−4.0
℃まで1日〜10日を費やして緩慢に冷却し、該冷却発
酵麦汁を過冷却状態にて流動させながら二次発酵工程に
供給し、発酵させることを特徴とする発酵麦芽飲料の製
造法。
1. A method for producing a fermented malt beverage, wherein the fermented wort obtained by fermenting wort in a primary fermentation step has a temperature range near freezing temperature of -1.0 to -4.0.
A method for producing a fermented malt beverage, characterized by slowly cooling to 1 ° C for 1 to 10 days , supplying the secondary fermentation step while flowing the cooled fermented wort in a supercooled state, and fermenting. .
【請求項2】 発酵麦芽飲料の製造法において、麦汁を
一次発酵工程にて発酵させることにより得られた発酵麦
汁を凍結温度付近の温度範囲である−1.0〜−4.0
℃まで1日〜10日を費やして緩慢に冷却し、該冷却発
酵麦汁を過冷却状態にて流動させた後、該過冷却状態の
発酵麦汁を濾過工程を経て二次発酵工程に供給し、新た
に醸造用酵母を添加して二次発酵を行うことを特徴とす
る発酵麦芽飲料の製造法。
2. The method for producing a fermented malt beverage, wherein the fermented wort obtained by fermenting the wort in the primary fermentation step is in the temperature range near the freezing temperature of -1.0 to -4.0.
After slowly cooling to 1 ° C for 1 to 10 days and flowing the cooled fermented wort in a supercooled state, the fermented wort in the supercooled state is supplied to a secondary fermentation step through a filtration step. Then, a method for producing a fermented malt beverage is characterized in that brewing yeast is newly added to carry out secondary fermentation.
JP15173994A 1994-06-10 1994-06-10 Production method of fermented malt beverage Expired - Fee Related JP3432599B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15173994A JP3432599B2 (en) 1994-06-10 1994-06-10 Production method of fermented malt beverage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15173994A JP3432599B2 (en) 1994-06-10 1994-06-10 Production method of fermented malt beverage

Publications (2)

Publication Number Publication Date
JPH07327656A JPH07327656A (en) 1995-12-19
JP3432599B2 true JP3432599B2 (en) 2003-08-04

Family

ID=15525233

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15173994A Expired - Fee Related JP3432599B2 (en) 1994-06-10 1994-06-10 Production method of fermented malt beverage

Country Status (1)

Country Link
JP (1) JP3432599B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5304384A (en) 1993-03-23 1994-04-19 Labatt Brewing Company Limited Improvements in production of fermented malt beverages

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5304384A (en) 1993-03-23 1994-04-19 Labatt Brewing Company Limited Improvements in production of fermented malt beverages

Also Published As

Publication number Publication date
JPH07327656A (en) 1995-12-19

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