JP7049821B2 - Method for manufacturing beer-like fermented malt beverage and method for improving foam retention of beer-like fermented malt beverage - Google Patents

Method for manufacturing beer-like fermented malt beverage and method for improving foam retention of beer-like fermented malt beverage Download PDF

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JP7049821B2
JP7049821B2 JP2017240962A JP2017240962A JP7049821B2 JP 7049821 B2 JP7049821 B2 JP 7049821B2 JP 2017240962 A JP2017240962 A JP 2017240962A JP 2017240962 A JP2017240962 A JP 2017240962A JP 7049821 B2 JP7049821 B2 JP 7049821B2
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久美子 猪本
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Description

本発明は、ビール様発酵麦芽飲料において、泡持ちを改善させるための特別な添加剤を使用することなく、泡持ちを向上させる方法に関する。 The present invention relates to a method for improving foam retention in a beer-like fermented malt beverage without the use of special additives for improving foam retention.

ビールや発泡酒等のビール様発酵麦芽飲料においては、泡は重要な外観品質である。泡品質は、主に、泡立ち、泡持ち、泡の付着性の点から評価される。ビールの泡は、主に麦芽由来のタンパク質によるものであり、タンパク質と泡品質についての関係性についても研究されている。例えば、ビールに塩基性アミノ酸(アルギニン、リジン、ヒスチジン)を添加すると泡の付着性が低下すること、すなわち、泡の付着性は、塩基性アミノ酸によって阻害されることが知られている(例えば、非特許文献1参照。)。 In beer-like fermented malt beverages such as beer and low-malt beer, foam is an important appearance quality. Foam quality is mainly evaluated in terms of foaming, foam retention, and foam adhesion. Beer foam is mainly due to malt-derived protein, and the relationship between protein and foam quality has also been studied. For example, it is known that the addition of basic amino acids (arginine, lysine, histidine) to beer reduces the adhesion of foam, that is, the adhesion of foam is inhibited by basic amino acids (eg,). See Non-Patent Document 1).

ビール様発酵麦芽飲料にタンパク質を補うことによって、泡品質を改善する方法が知られている。例えば、発泡性飲料に酵母懸濁液の上清から得られる分子量50kDa以上の成分を配合することにより、泡持ちを改善する方法や(例えば、特許文献1参照。)、発泡性飲料に、大麦のプロテアーゼ処理物であって、分子量が10~25kDaのポリペプチドを含み、プロリン含有量が13.5モル%以上である疎水性ポリペプチド混合物を配合することにより、泡持ちを改善する方法や(例えば、特許文献2参照。)が知られている。タンパク質を添加する方法以外では、例えば、発酵液に消泡剤を添加することによってアルコール発酵中の液面での泡の形成を抑制することにより、得られる発酵飲料の泡持ちを改善する方法がある(例えば、特許文献3参照。)。 There are known ways to improve foam quality by supplementing beer-like fermented malt beverages with protein. For example, a method for improving foam retention by blending a component having a molecular weight of 50 kDa or more obtained from the supernatant of a yeast suspension into an effervescent beverage (see, for example, Patent Document 1), or barley in an effervescent beverage. A method for improving foam retention by blending a hydrophobic polypeptide mixture containing a polypeptide having a molecular weight of 10 to 25 kDa and having a proline content of 13.5 mol% or more. For example, see Patent Document 2). Other than the method of adding protein, for example, there is a method of improving the foam retention of the obtained fermented beverage by suppressing the formation of foam on the liquid surface during alcoholic fermentation by adding an antifoaming agent to the fermented liquid. (See, for example, Patent Document 3).

特開2015-223140号公報Japanese Unexamined Patent Publication No. 2015-223140 特許第5687629号公報Japanese Patent No. 5687629 特開2016-152778号公報Japanese Unexamined Patent Publication No. 2016-152778

ビール酒造組合編、「ビールの基本技術」、公益財団法人日本醸造協会発行、2002年、第127ページ。Beer Brewing Association, "Basic Technology of Beer", published by the Brewing Society of Japan, 2002, p. 127.

本発明は、泡持ちを改善させるための特別な添加剤を使用することなく、泡持ちが改善されたビール様発酵麦芽飲料を提供することを目的とする。 It is an object of the present invention to provide a beer-like fermented malt beverage with improved foam retention without the use of special additives for improving foam retention.

本発明者は、上記課題を解決すべく鋭意研究した結果、仕込工程におけるタンパク質分解処理や煮沸処理の条件、発酵条件、及び熟成条件を最適化し、かつ発酵工程又は熟成工程中に発酵槽又は貯酒槽の底に沈殿した酵母を除去することによって、製造されるビール様発酵麦芽飲料中の泡持ちに影響するアミノ酸の含有量を低く抑えることができ、泡持ちを向上させられることを見出し、本発明を完成させた。 As a result of diligent research to solve the above problems, the present inventor has optimized the conditions for protein decomposition treatment and boiling treatment in the preparation process, fermentation conditions, and aging conditions, and has made the fermentation tank or liquor storage during the fermentation process or aging process. We found that by removing the yeast that had settled at the bottom of the tank, the content of amino acids that affect the foam retention in the produced beer-like fermented malt beverage could be kept low, and the foam retention could be improved. Completed the invention.

本発明に係るビール様発酵麦芽飲料の製造方法及びビール様発酵麦芽飲料の泡持ち向上方法は、下記[1]~[]である。
[1] 麦芽を含む発酵原料と原料水とを含む混合物を50℃超、60℃以下で30分間~90分間保持してタンパク質を分解させた後、60℃超90℃未満で糖化処理した後、得られた糖液を煮沸処理し、発酵原料液を調製する仕込工程と、
前記仕込工程で調製された発酵原料液に下面発酵酵母を接種して、発酵槽中で9℃超、12℃以下で発酵を行う発酵工程と、
発酵工程により得られた発酵液を、貯酒槽中で3~7日間熟成させる熟成工程と、
を有し、
前記煮沸処理の煮沸時間が30分間以上100分間未満であり、
前記糖液のpHが5.3~5.8であり、
前記発酵工程から前記熟成工程が終了するまでに、前記発酵槽又は前記貯酒槽の底に沈降した酵母を、少なくとも1回は除去し、
製造されたビール様発酵麦芽飲料のPierce 660 nm Protein Assayにより測定されるタンパク質濃度が150~180mg/Lであり、かつグルタミン、グルタミン酸、グリシン、イソロイシン、γ-アミノ酪酸、及びプロリンの合計含有量が34mg/100mL以下となるように調整することを特徴とする、ビール様発酵麦芽飲料の製造方法。
[2] 前記発酵原料の全量に対する麦芽の比率が50質量%以上である、前記[1]のビール様発酵麦芽飲料の製造方法。
] 製造されたビール様発酵麦芽飲料のアルギニン、リジン、及びヒスチジンの合計含有量が2.0mg/100mL以下となるように調整する、前記[1]又は[2]のビール様発酵麦芽飲料の製造方法。
] 製造されたビール様発酵麦芽飲料のNIBEM値が260秒以上となるように調整する、前記[1]~[]のいずれかのビール様発酵麦芽飲料の製造方法。
] 発酵原料の全量に対する麦芽の比率が50質量%以上であり、発酵工程を経て製造されるビール様発酵麦芽飲料の泡持ちを向上させる方法であって、
ビール様発酵麦芽飲料中のPierce 660 nm Protein Assayにより測定されるタンパク質濃度を150~180mg/Lとし、グルタミン、グルタミン酸、グリシン、イソロイシン、γ-アミノ酪酸、及びプロリンの合計含有量を34mg/100mL以下に調整することを特徴とする、ビール様発酵麦芽飲料の泡持ち向上方法。
The method for producing a beer-like fermented malt beverage and the method for improving the foam retention of the beer-like fermented malt beverage according to the present invention are as follows [1] to [ 5 ].
[1] A mixture containing a fermentation raw material containing malt and raw water is held at a temperature of more than 50 ° C. and 60 ° C. or lower for 30 to 90 minutes to decompose proteins, and then saccharified at a temperature of more than 60 ° C. and less than 90 ° C. , The preparation process of boiling the obtained sugar solution to prepare the fermentation raw material solution,
A fermentation step in which bottom-fermenting yeast is inoculated into the fermentation raw material liquid prepared in the above-mentioned preparation step and fermentation is performed in a fermenter at a temperature of more than 9 ° C and less than 12 ° C.
A aging process in which the fermented liquid obtained in the fermentation process is aged in a liquor tank for 3 to 7 days.
Have,
The boiling time of the boiling treatment is 30 minutes or more and less than 100 minutes.
The pH of the sugar solution is 5.3 to 5.8, and the pH is 5.3 to 5.8.
From the fermentation step to the end of the aging step, the yeast that has settled in the bottom of the fermentation tank or the liquor storage tank is removed at least once.
The produced beer-like fermented malt beverage has a protein concentration of 150-180 mg / L as measured by the Pierce 660 nm Protein Assay and a total content of glutamine, glutamic acid, glycine, isoleucine, γ-aminobutyric acid, and proline. A method for producing a beer-like fermented malt beverage, which comprises adjusting the content to 34 mg / 100 mL or less .
[2] The method for producing a beer-like fermented malt beverage according to the above [1], wherein the ratio of malt to the total amount of the fermentation raw material is 50% by mass or more.
[ 3 ] The beer-like fermented malt beverage according to the above [1] or [2] , wherein the total content of arginine, lysine, and histidine of the produced beer-like fermented malt beverage is adjusted to 2.0 mg / 100 mL or less. Manufacturing method.
[ 4 ] The method for producing a beer-like fermented malt beverage according to any one of [1] to [ 3 ] above, wherein the NIBEM value of the produced beer-like fermented malt beverage is adjusted to be 260 seconds or longer.
[ 5 ] A method for improving the foam retention of a beer-like fermented malt beverage produced through a fermentation step, in which the ratio of malt to the total amount of fermentation raw materials is 50% by mass or more.
The protein concentration measured by the Pierce 660 nm Protein Assay in the beer-like fermented malt beverage is 150 to 180 mg / L, and the total content of glutamine, glutamic acid, glycine, isoleucine, γ-aminobutyric acid, and proline is 34 mg / 100 mL or less. A method for improving the foam retention of beer-like fermented malt beverages, which is characterized by adjusting to.

本発明により、麦芽を含む発酵原料を用いて発酵工程を経て製造される、泡持ちの良好なビール様発酵麦芽飲料が製造できる。 INDUSTRIAL APPLICABILITY According to the present invention, a beer-like fermented malt beverage having good foam retention, which is produced through a fermentation step using a fermentation raw material containing malt, can be produced.

本発明及び本願明細書において、「ビール様発酵麦芽飲料」とは、発酵原料の少なくとも一部が麦芽であって、発酵工程を経て製造された飲料であって、アルコール含有量に関わらず、ビールと同等の又はそれと似た風味・味覚及びテクスチャーを有し、高い止渇感・ドリンカビリティーを有する発泡性飲料を意味する。すなわち、ビール様発酵麦芽飲料は、アルコール飲料であってもよく、アルコール含量が1容量%未満であるいわゆるノンアルコール飲料又はローアルコール飲料であってもよい。ビール様発酵麦芽飲料としては、具体的には、ビール、発泡酒、ローアルコールビール、ノンアルコールビール等が挙げられる。その他、麦芽を原料とし、発酵工程を経て製造された飲料を、アルコール含有蒸留液と混和して得られたリキュール類であってもよい。アルコール含有蒸留液とは、蒸留操作により得られたアルコールを含有する溶液であり、例えば、原料用アルコールであってもよく、スピリッツ、ウィスキー、ブランデー、ウオッカ、ラム、テキーラ、ジン、焼酎等の蒸留酒等を用いることができる。 In the present invention and the present specification, the "beer-like fermented malt beverage" is a beverage produced by having at least a part of the fermentation raw material malt and undergoing a fermentation step, regardless of the alcohol content. It means an effervescent beverage having a flavor, taste and texture equivalent to or similar to that of, and having a high feeling of thirst and drinkability. That is, the beer-like fermented malt beverage may be an alcoholic beverage, or may be a so-called non-alcoholic beverage or a low-alcoholic beverage having an alcohol content of less than 1% by volume. Specific examples of the beer-like fermented malt beverage include beer, low-malt beer, low-alcoholic beer, and non-alcoholic beer. In addition, liqueurs obtained by mixing a beverage produced from malt as a raw material through a fermentation step with an alcohol-containing distillate may be used. The alcohol-containing distillate is a solution containing alcohol obtained by a distillation operation, and may be, for example, alcohol for raw materials. Distillation of spirits, whiskey, brandy, wokca, lamb, tequila, gin, shochu, etc. Alcohol and the like can be used.

後記参考例で示すように、アルギニン、リジン、ヒスチジンといった塩基性アミノ酸以外にもいくつかのアミノ酸は、ビール様発酵麦芽飲料の泡持ちに影響を与える。具体的には、グルタミン酸、グルタミン、グリシン、イソロイシン、プロリン、及びγ-アミノ酪酸(GABA)は、飲料中の含有量依存的に、泡持ちが低下する傾向がある。塩基性アミノ酸以外のアミノ酸が、ビール様発酵麦芽飲料の泡持ちに影響を与えることは、本発明者らにより初めて見いだされた知見である。なお、以降の明細書において、アルギニン、リジン、ヒスチジン、グルタミン酸、グルタミン、グリシン、イソロイシン、プロリン、及びGABAは、「泡影響アミノ酸」と称することがある。 As shown in the reference examples below, some amino acids other than basic amino acids such as arginine, lysine, and histidine affect the foam retention of beer-like fermented malt beverages. Specifically, glutamic acid, glutamine, glycine, isoleucine, proline, and γ-aminobutyric acid (GABA) tend to have a reduced foam retention depending on the content in the beverage. It is the first finding by the present inventors that amino acids other than basic amino acids affect the foam retention of beer-like fermented malt beverages. In the following specification, arginine, lysine, histidine, glutamic acid, glutamine, glycine, isoleucine, proline, and GABA may be referred to as "foam-affecting amino acids".

ビールの泡持ちには、主に麦芽に由来する泡形成に関与するタンパク質(起泡タンパク質)が十分量含まれていることと、泡持ちを低下させるアミノ酸が少ないことが重要である。具体的には、ビール様発酵麦芽飲料の泡持ちを向上させるためには、最終製品たる飲料中に適切な量の起泡タンパク質を残存させつつ、発酵工程では確実に発酵原料液中のアミノ酸を酵母に取り込み、最終製品に残存するアミノ酸量を低減させることが重要である。本発明においては、仕込工程におけるタンパク質分解及び煮沸処理の条件、発酵工程における発酵条件、及び熟成工程における熟成条件をそれぞれ調整し、かつ発酵工程又は熟成工程中に発酵槽又は貯酒槽の底に沈殿した酵母を除去することによって、製造されるビール様発酵麦芽飲料中の総タンパク質量は低減させることなく、泡持ちに影響するアミノ酸の含有量を低く抑え、泡持ちを向上させることができる。 It is important that the foam retention of beer contains a sufficient amount of protein (foaming protein) mainly derived from malt and is involved in foam formation, and that there are few amino acids that reduce foam retention. Specifically, in order to improve the foam retention of beer-like fermented malt beverages, while leaving an appropriate amount of foamed protein in the beverage, which is the final product, the amino acids in the fermentation raw material liquid are surely used in the fermentation process. It is important to incorporate it into yeast and reduce the amount of amino acids remaining in the final product. In the present invention, the conditions for protein decomposition and boiling treatment in the preparation step, the fermentation conditions in the fermentation step, and the aging conditions in the aging step are adjusted, and the fermentation conditions are settled at the bottom of the fermenter or the liquor tank during the fermentation step or the aging step. By removing the yeast, the content of amino acids that affect the foam retention can be kept low and the foam retention can be improved without reducing the total protein content in the produced beer-like fermented malt beverage.

具体的には、本発明に係るビール様発酵麦芽飲料の製造方法(以下、「本発明に係る製造方法」ということがある。)は、麦芽を含む発酵原料と原料水とを含む混合物を糖化処理した後、得られた糖液を煮沸処理し、発酵原料液を調製する仕込工程(発酵原料液調製工程)と、仕込工程で調製された発酵原料液に下面発酵酵母を接種して、発酵を行う発酵工程と、発酵工程により得られた発酵液を、熟成させる熟成工程と、を有し、かつ各工程の条件を特定の範囲内に調整した方法である。以下、一般的なビール様発酵麦芽飲料の製造方法に本発明に係る低減方法を適用した方法を説明する。 Specifically, the method for producing a beer-like fermented malt beverage according to the present invention (hereinafter, may be referred to as "the production method according to the present invention") is a saccharification of a mixture containing a fermentation raw material containing malt and raw water. After the treatment, the obtained sugar solution is boiled to prepare a fermentation raw material solution (fermentation raw material solution preparation step), and the fermentation raw material solution prepared in the preparation step is inoculated with bottom fermenting yeast for fermentation. This method has a fermentation step of performing the above-mentioned step and a ripening step of aging the fermented liquid obtained by the fermentation step, and the conditions of each step are adjusted within a specific range. Hereinafter, a method in which the reduction method according to the present invention is applied to a general method for producing a beer-like fermented malt beverage will be described.

まず、仕込工程として、麦芽を含む発酵原料と原料水から発酵原料液を調製する。具体的には、発酵原料と原料水を含む混合物に対してタンパク質分解処理を行った後、糖化処理を行って当該混合物中の澱粉質を糖化し、糖化液を得る。発酵原料としては、麦芽のみを用いてもよく、麦芽と麦芽以外の穀物原料のみを用いてもよく、麦芽と糖質原料を用いてもよい。 First, as a preparation step, a fermentation raw material liquid is prepared from a fermentation raw material containing malt and raw material water. Specifically, a mixture containing a fermentation raw material and raw material water is subjected to a proteolytic treatment and then a saccharification treatment to saccharify the starch in the mixture to obtain a saccharified solution. As the fermentation raw material, only malt may be used, only malt and grain raw materials other than malt may be used, or malt and sugar raw materials may be used.

原料として用いる麦芽は、麦芽粉砕物が好ましい。麦芽粉砕物は、大麦、例えば二条大麦を、常法により発芽させ、これを乾燥後、所定の粒度に粉砕することにより得られる。粉砕処理は、常法により行うことができる。 The malt used as a raw material is preferably a crushed malt product. The crushed malt product is obtained by germinating barley, for example, Nijo barley by a conventional method, drying the barley, and then pulverizing the malt to a predetermined particle size. The pulverization treatment can be performed by a conventional method.

麦芽以外の穀物原料としては、例えば、大麦や小麦等の麦類、米、トウモロコシ、大豆等の豆類、イモ類等が挙げられる。麦芽以外の穀物原料は、穀物シロップ、穀物エキス等として用いることもできるが、粉砕処理して得られる穀物粉砕物として用いることが好ましい。また、コーンスターチ、コーングリッツ等のように、粉砕処理の前後において通常なされる処理を施したものであってもよい。糖質原料としては、例えば、液糖等の糖類が挙げられる。 Examples of grain raw materials other than malt include wheat such as barley and wheat, beans such as rice, corn and soybean, and potatoes. Grain raw materials other than malt can be used as grain syrup, grain extract and the like, but are preferably used as grain crushed products obtained by crushing. Further, cornstarch, corn grits and the like may be subjected to a treatment usually performed before and after the crushing treatment. Examples of the sugar raw material include sugars such as liquid sugar.

ビール様発酵麦芽飲料中のアミノ酸は、主に原料に由来するため、麦芽のようにアミノ酸を多く含有する発酵原料の使用比率が高いほど、最終的に得られるビール様発酵麦芽飲料中のアミノ酸の含有量は多くなる傾向にあり、当然に泡影響アミノ酸の含有量も多くなる。本発明に係る製造方法は、最終製品であるビール様発酵麦芽飲料に持ち込まれる原料に由来する泡影響アミノ酸の量を抑制することができるため、発酵原料に対する麦芽の使用比率が高いビール様発酵麦芽飲料の製造に適している。本発明に係る製造方法において、麦芽使用比率(発酵原料の全量に対する麦芽の使用量の割合)は、50質量%以上であることが好ましく、75質量%以上であることがより好ましく、80質量%以上であることがさらに好ましく、100質量%であることが特に好ましい。 Since the amino acids in the beer-like fermented malt beverage are mainly derived from the raw materials, the higher the ratio of the fermented raw materials containing a large amount of amino acids such as malt, the more the amino acids in the finally obtained beer-like fermented malt beverage. The content tends to increase, and naturally the content of foam-affecting amino acids also increases. The production method according to the present invention can suppress the amount of foam-affected amino acids derived from the raw material brought into the final product, beer-like fermented malt beverage, and therefore the ratio of malt used to the fermented raw material is high. Suitable for making beverages. In the production method according to the present invention, the malt use ratio (ratio of the amount of malt used to the total amount of fermentation raw materials) is preferably 50% by mass or more, more preferably 75% by mass or more, and more preferably 80% by mass. The above is more preferable, and 100% by mass is particularly preferable.

発酵原料と原料水とを含む混合物には、その他の副原料を加えてもよい。当該副原料としては、例えば、食物繊維、酵母エキス、果汁、苦味料、着色料、香草、香料等が挙げられる。また、必要に応じて、α-アミラーゼ、グルコアミラーゼ、プルラナーゼ等の糖化酵素やプロテアーゼ等の酵素剤を添加することができる。 Other auxiliary ingredients may be added to the mixture containing the fermentation ingredient and the feedstock water. Examples of the auxiliary raw material include dietary fiber, yeast extract, fruit juice, bitterness, coloring agent, fragrance, and fragrance. Further, if necessary, a saccharifying enzyme such as α-amylase, glucoamylase, and pullulanase, or an enzyme agent such as a protease can be added.

タンパク質分解処理時の温度と時間の条件は、発酵原料中のタンパク質の分解の程度に影響を及ぼす。本発明に係る製造方法においては、タンパク質分解処理は、発酵原料と原料水と、必要に応じてその他の原料を含む混合物を、50℃超、60℃以下で30分間~90分間保持して行う。タンパク質の分解処理は、麦芽由来の酵素や、別途添加した酵素を利用して行う。タンパク質の分解処理の温度と時間を前記範囲内に調整することにより、起泡タンパク質の含有量が多く、アミノ酸含有量が十分に抑えられたビール様発酵麦芽飲料が得られる。本発明に係る製造方法におけるタンパク質分解処理の温度と時間は、52~60℃で30分間~90分間が好ましく、52~58℃で30分間~90分間がより好ましく、52~58℃で45分間~75分間がさらに好ましい。 Temperature and time conditions during the proteolysis process affect the degree of protein degradation in the fermentation feedstock. In the production method according to the present invention, the proteolytic treatment is carried out by holding a mixture containing a fermentation raw material, raw water and, if necessary, other raw materials at a temperature of more than 50 ° C. and 60 ° C. or lower for 30 to 90 minutes. .. The protein decomposition treatment is carried out using an enzyme derived from malt or an enzyme added separately. By adjusting the temperature and time of the protein decomposition treatment within the above range, a beer-like fermented malt beverage having a high content of foaming protein and a sufficiently suppressed amino acid content can be obtained. The temperature and time of the proteolysis treatment in the production method according to the present invention are preferably 52 to 60 ° C. for 30 to 90 minutes, more preferably 52 to 58 ° C. for 30 to 90 minutes, and 52 to 58 ° C. for 45 minutes. -75 minutes is more preferred.

タンパク質を分解させた後の混合物を、さらに60℃超90℃未満で保持して糖化処理する。糖化処理は、麦芽由来の酵素や、別途添加した酵素を利用して行う。糖化処理時の温度や時間は、発酵原料全体に占める麦芽の割合、添加した酵素の種類や混合物の量、目的とするビール様発酵麦芽飲料の品質等を考慮して、適宜調整される。例えば、糖化処理は、タンパク質分解処理後の混合物を、60℃超70℃以下で20~60分間保持する等、常法により行うことができる。 The mixture after decomposing the protein is further held at more than 60 ° C and lower than 90 ° C for saccharification treatment. The saccharification treatment is carried out using an enzyme derived from malt or an enzyme added separately. The temperature and time during the saccharification treatment are appropriately adjusted in consideration of the ratio of malt to the total fermentation raw material, the type and amount of the added enzyme, the quality of the target beer-like fermented malt beverage, and the like. For example, the saccharification treatment can be carried out by a conventional method, such as holding the mixture after the proteolysis treatment at a temperature of more than 60 ° C. and 70 ° C. or lower for 20 to 60 minutes.

糖化処理後に得られた糖液を煮沸処理することにより、発酵原料液(麦汁)を調製することができる。糖液は、煮沸処理前に濾過し、得られた濾液を煮沸処理することが好ましい。また、この糖液の濾液に替わりに、麦芽エキスに温水を加えたものを用い、これを煮沸してもよい。 A fermentation raw material liquid (wort) can be prepared by boiling the sugar liquid obtained after the saccharification treatment. It is preferable that the sugar solution is filtered before the boiling treatment and the obtained filtrate is boiled. Further, instead of the filtrate of this sugar solution, a malt extract to which warm water is added may be used and boiled.

本発明に係る製造方法においては、煮沸処理に供される糖液のpHは、5.3~5.8の範囲内とする。糖化処理後に得られた糖液のpHが前記範囲内にない場合には、有機酸やアルカリ等のpH調整剤を添加してpHを調整する。また、煮沸処理の煮沸時間は、30分間以上100分間未満であり、30~90分間が好ましく、45~70分間がより好ましい。pHが前記範囲内にある状態で前記範囲内の時間煮沸処理を行うことにより、起泡タンパク質が過剰に凝集して不溶化することが抑制され、起泡タンパク質の含有量が十分なビール様発酵麦芽飲料が得られる。 In the production method according to the present invention, the pH of the sugar solution subjected to the boiling treatment is in the range of 5.3 to 5.8. If the pH of the sugar solution obtained after the saccharification treatment is not within the above range, a pH adjuster such as an organic acid or an alkali is added to adjust the pH. The boiling time of the boiling treatment is 30 minutes or more and less than 100 minutes, preferably 30 to 90 minutes, and more preferably 45 to 70 minutes. By performing the boiling treatment within the above range while the pH is within the above range, excessive aggregation and insolubilization of the foaming protein is suppressed, and the beer-like fermented malt having a sufficient content of the foaming protein is suppressed. Beverages are obtained.

煮沸処理前又は煮沸処理中に、香草等を適宜添加することにより、所望の香味を有するビール様発酵麦芽飲料を製造することができる。特にホップは、煮沸処理前又は煮沸処理中に添加することが好ましい。ホップの存在下で煮沸処理することにより、ホップの風味・香気成分を効率よく煮出することができる。ホップの添加量、添加態様(例えば数回に分けて添加するなど)及び添加時期は、適宜決定することができる。 By appropriately adding flavors and the like before or during the boiling treatment, a beer-like fermented malt beverage having a desired flavor can be produced. In particular, hops are preferably added before or during the boiling process. By boiling in the presence of hops, the flavor and aroma components of hops can be efficiently boiled. The amount of hops added, the mode of addition (for example, addition in several portions) and the timing of addition can be appropriately determined.

仕込工程後、発酵工程前に、調製された発酵原料液から、沈殿により生じたタンパク質等の粕を除去することが好ましい。粕の除去は、いずれの固液分離処理で行ってもよいが、一般的には、ワールプールと呼ばれる槽を用いて沈殿物を除去する。この際の発酵原料液の温度は、15℃以上であればよく、一般的には50~80℃程度で行われる。粕を除去した後の発酵原料液(濾液)は、プレートクーラー等により適切な発酵温度まで冷却する。 After the charging step and before the fermentation step, it is preferable to remove the residue such as protein generated by the precipitation from the prepared fermentation raw material liquid. The lees may be removed by any solid-liquid separation treatment, but generally, the precipitate is removed using a tank called a whirlpool. The temperature of the fermentation raw material liquid at this time may be 15 ° C. or higher, and is generally about 50 to 80 ° C. After removing the residue, the fermentation raw material liquid (filtrate) is cooled to an appropriate fermentation temperature by a plate cooler or the like.

次いで、発酵工程として、冷却した発酵原料液に下面発酵酵母を接種して、発酵槽中で発酵を行う。冷却した発酵原料液は、そのまま発酵工程に供してもよく、所望のエキス濃度に調整した後に発酵工程に供してもよい。発酵に用いる下面発酵酵母は特に限定されるものではなく、通常、酒類の製造に用いられる酵母の中から適宜選択して用いることができる。 Next, as a fermentation step, the cooled fermentation raw material liquid is inoculated with bottom-fermenting yeast and fermented in a fermenter. The cooled fermentation raw material liquid may be subjected to the fermentation step as it is, or may be subjected to the fermentation step after adjusting to a desired extract concentration. The bottom-fermenting yeast used for fermentation is not particularly limited, and usually, it can be appropriately selected and used from yeasts used for producing alcoholic beverages.

本発明に係る製造方法においては、発酵温度は、9℃超、12℃以下とし、10~12℃が好ましい。前記温度範囲内で発酵を行うことにより、酵母によるアミノ酸の取り込みがより効率よく行われ、泡影響アミノ酸の含有量が十分に低減されたビール様発酵麦芽飲料が得られる。発酵時間は特に限定されるものではないが、9日間以内であることが好ましく、8日間以内であることがより好ましく、7日間以内であることがさらに好ましい。 In the production method according to the present invention, the fermentation temperature is preferably more than 9 ° C. and 12 ° C. or lower, preferably 10 to 12 ° C. By fermenting within the above temperature range, the uptake of amino acids by yeast is performed more efficiently, and a beer-like fermented malt beverage having a sufficiently reduced content of foam-affecting amino acids can be obtained. The fermentation time is not particularly limited, but is preferably 9 days or less, more preferably 8 days or less, and even more preferably 7 days or less.

発酵工程後、得られた発酵液を、貯酒槽中で3~7日間、9~12℃で、香味が安定するまで熟成させ(熟成工程)、その後、0℃程度の低温条件下で3~7日間貯蔵し安定化させる(安定化工程)。この熟成工程と安定化工程をあわせて、貯酒工程という。熟成期間を3~7日間と比較的短くすることにより、製造されるビール様発酵麦芽飲料中の総タンパク質量は低減させることなく、泡影響アミノ酸の含有量を低く抑えることができる。 After the fermentation step, the obtained fermented liquor is aged in a liquor tank for 3 to 7 days at 9 to 12 ° C. until the flavor is stable (aging step), and then under low temperature conditions of about 0 ° C. for 3 to 3 to Store for 7 days to stabilize (stabilization step). This aging process and stabilization process are collectively called the sake storage process. By relatively shortening the aging period to 3 to 7 days, the content of foam-affecting amino acids can be kept low without reducing the total amount of protein in the produced beer-like fermented malt beverage.

その後、濾過工程として、熟成後の発酵液を濾過することにより、酵母及び当該温度域で不溶なタンパク質等を除去して、目的のビール様発酵麦芽飲料を得ることができる。当該濾過処理は、酵母を濾過除去可能な手法であればよく、例えば、珪藻土濾過、平均孔径が0.4~0.6μm程度のフィルターによるフィルター濾過等が挙げられる。 Then, as a filtration step, by filtering the fermented liquid after aging, yeast and insoluble proteins in the temperature range can be removed to obtain the desired beer-like fermented malt beverage. The filtration treatment may be any method as long as it can filter and remove yeast, and examples thereof include diatomaceous earth filtration and filter filtration with a filter having an average pore size of about 0.4 to 0.6 μm.

本発明に係る製造方法においては、下面発酵酵母を用いているため、発酵工程又は熟成工程中において、活性が低下した酵母や死滅した酵母は、発酵槽又は貯酒槽の底部に沈殿する。死滅した酵母は、その後自己消化され、内包されていたアミノ酸やプロテアーゼが発酵液中に放出される結果、発酵液中の起泡タンパク質が分解され、また、アミノ酸含有量は増大する。本発明に係る製造方法においては、発酵工程又は熟成工程中に、すなわち、発酵工程から熟成工程が終了するまでに、発酵槽又は貯酒槽の底に沈降した酵母を、少なくとも1回は除去する。沈降した酵母の除去は、発酵工程のみで行われてもよく、熟成工程のみで行われてもよく、発酵工程と熟成工程の両方で行われてもよい。発酵槽からの酵母の除去は、発酵槽の底部又はその近傍から、沈降している酵母を排出させることにより行うことができる。発酵槽の底に沈降した酵母の除去は、例えば、一定の時間ごとに行ってもよく、沈降した酵母が一定の量に達した時点で行ってもよい。貯酒槽からの酵母の除去は、発酵槽からの酵母の除去と同様にして行うことができる。 Since the bottom-fermenting yeast is used in the production method according to the present invention, yeast whose activity has decreased or which has died during the fermentation step or the aging step precipitates at the bottom of the fermenter or the liquor storage tank. The dead yeast is then autolyzed, and the contained amino acids and proteases are released into the fermented liquor. As a result, the foaming protein in the fermented liquor is decomposed and the amino acid content is increased. In the production method according to the present invention, yeast that has settled at the bottom of the fermentation tank or the liquor storage tank is removed at least once during the fermentation step or the aging step, that is, from the fermentation step to the end of the aging step. The removal of the precipitated yeast may be carried out only in the fermentation step, may be carried out only in the aging step, or may be carried out in both the fermentation step and the ripening step. The removal of yeast from the fermenter can be performed by discharging the yeast that has settled from the bottom of the fermenter or its vicinity. The yeast that has settled at the bottom of the fermenter may be removed, for example, at regular intervals, or when the amount of yeast that has settled reaches a certain amount. The removal of yeast from the liquor tank can be performed in the same manner as the removal of yeast from the fermenter.

本発明に係る製造方法においては、前述の通り、タンパク質分解処理等の条件を調整することによって、十分量の起泡タンパク質を含有し、かつ泡影響アミノ酸含有量が低いビール様発酵麦芽飲料が得られる。本発明に係る製造方法により製造されたビール様発酵麦芽飲料のタンパク質含有量としては、Pierce 660 nm Protein Assayにより測定されるタンパク質濃度が150~180mg/Lであることが好ましい。Pierce 660 nm Protein Assay は、Pierce 660nm Protein Assay Reagent(Thermo Scientific社製)がタンパク質と結合することで極大吸収波長が660nmにシフトする化学反応を利用した測定方法である。 In the production method according to the present invention, as described above, by adjusting the conditions such as proteolysis treatment, a beer-like fermented malt beverage containing a sufficient amount of foaming protein and having a low content of foam-affecting amino acids can be obtained. Will be. As for the protein content of the beer-like fermented malt beverage produced by the production method according to the present invention, the protein concentration measured by the Pierce 660 nm Protein Assay is preferably 150 to 180 mg / L. The Pierce 660 nm Protein Assay is a measurement method that utilizes a chemical reaction in which the maximum absorption wavelength shifts to 660 nm when the Pierce 660 nm Protein Assay Reagent (manufactured by Thermo Scientific) binds to a protein.

また、本発明に係る製造方法により製造されたビール様発酵麦芽飲料は、塩基性アミノ酸以外の泡影響アミノ酸の総量、すなわち、グルタミン、グルタミン酸、グリシン、イソロイシン、GABA、及びプロリンの合計含有量が、36mg/100mL以下であることが好ましく、34mg/100mL以下であることがより好ましい。当該ビール様発酵麦芽飲料は、塩基性アミノ酸の総量、すなわち、であるアルギニン、リジン、及びヒスチジンの合計含有量が、2.2mg/100mL以下であることが好ましく、2.0mg/100mL以下であることがより好ましい。 In addition, the beer-like fermented malt beverage produced by the production method according to the present invention has a total amount of foam-affecting amino acids other than basic amino acids, that is, a total content of glutamine, glutamic acid, glycine, isoleucine, GABA, and proline. It is preferably 36 mg / 100 mL or less, and more preferably 34 mg / 100 mL or less. The beer-like fermented malt beverage preferably has a total amount of basic amino acids, that is, a total content of arginine, lysine, and histidine of 2.2 mg / 100 mL or less, preferably 2.0 mg / 100 mL or less. Is more preferable.

なお、ビール様発酵麦芽飲料中の各アミノ酸の含有量は、例えば、(米国)ウォーターズ社製Acquity UPLC分析装置を用いて、アキュタグウルトラ(AccQ-Tag Ultra)ラベル化法により測定することができる。また、日本電子社製アミノ酸自動分析装置JLC―500/V型などを用いて測定することも可能である。 The content of each amino acid in the beer-like fermented malt beverage can be measured by, for example, an Acquity UPLC analyzer manufactured by Waters (USA) by the Accutag Ultra (AccQ-Tag Ultra) labeling method. .. It is also possible to measure using an automatic amino acid analyzer JLC-500 / V type manufactured by JEOL Ltd.

本発明に係る製造方法により製造されたビール様発酵麦芽飲料は、同じ発酵原料を用いて従来の製造条件で製造されたビール様発酵麦芽飲料よりも、泡持ちが向上している。本発明に係る製造方法により製造されたビール様発酵麦芽飲料のNIBEM値は、260秒以上であることが好ましく、260~280秒であることがより好ましい。なお、NIBEM値は、注がれた泡の崩壊速度を電気伝導度で測定したものであり、ビール等の泡持ち評価に一般的に用いられているものである。ビール様発酵麦芽飲料のNIBEM値は、EBC(European Brewery Convention)のAnalytica-EBC標準法、又はこれに準じた方法により測定できる。 The beer-like fermented malt beverage produced by the production method according to the present invention has improved foam retention as compared with the beer-like fermented malt beverage produced under the conventional production conditions using the same fermentation raw material. The NIBEM value of the beer-like fermented malt beverage produced by the production method according to the present invention is preferably 260 seconds or longer, and more preferably 260 to 280 seconds. The NIBEM value is a measurement of the disintegration rate of the poured foam by electrical conductivity, and is generally used for evaluating the foam retention of beer and the like. The NIBEM value of the beer-like fermented malt beverage can be measured by the Analytica-EBC standard method of EBC (European Brewery Convention) or a method similar thereto.

次に実施例及び参考例を示して本発明をさらに詳細に説明するが、本発明は以下の実施例等に限定されるものではない。 Next, the present invention will be described in more detail with reference to Examples and Reference Examples, but the present invention is not limited to the following Examples and the like.

<ビール様発酵麦芽飲料の総タンパク質濃度の測定>
ビール様発酵麦芽飲料の総タンパク質濃度は、Pierce 660nm Protein Assayにより行った。具体的には、サンプル100μLに、Pierce 660nm Protein Assay Reagent(Thermo Scientific社製)1.5mLを添加し、室温で5分間保持した後、分光光度計を用いて660nmの吸光度を測定した。濃度既知のBSAタンパク質を用いて予め作成した検量線と、660nmの吸光度値に基づいて、各サンプルの総タンパク質濃度(mg/L)を求めた。
<Measurement of total protein concentration of beer-like fermented malt beverage>
The total protein concentration of the beer-like fermented malt beverage was measured by the Pierce 660nm Protein Assay. Specifically, 1.5 mL of Pierce 660 nm Protein Assay Reagent (manufactured by Thermo Scientific) was added to 100 μL of the sample, and the mixture was held at room temperature for 5 minutes, and then the absorbance at 660 nm was measured using a spectrophotometer. The total protein concentration (mg / L) of each sample was determined based on a calibration curve prepared in advance using a BSA protein having a known concentration and an absorbance value of 660 nm.

<NIBEM値>
ビール様発酵麦芽飲料のNIBEM値は、NIBEM測定機器(Haffmans社製)を使用して測定した。
<NIBEM value>
The NIBEM value of the beer-like fermented malt beverage was measured using a NIBEM measuring device (manufactured by Haffmans).

<ビール様発酵麦芽飲料の各アミノ酸の濃度の測定>
ビール様発酵麦芽飲料中の各アミノ酸は、(米国)ウォーターズ社製Acquity UPLC分析装置を用いて、アキュタグウルトラ(AccQ-Tag Ultra)ラベル化法により測定した。検量線は、アミノ酸混合標準液H型(和光純薬社製)を用いて作成した。
<Measurement of the concentration of each amino acid in beer-like fermented malt beverage>
Each amino acid in the beer-like fermented malt beverage was measured by the Accutag Ultra (AccQ-Tag Ultra) labeling method using an Acquity UPLC analyzer manufactured by Waters, USA. The calibration curve was prepared using an amino acid mixed standard solution H type (manufactured by Wako Pure Chemical Industries, Ltd.).

[参考例1]
市販のビールに各アミノ酸を添加し、泡持ちに対する影響を調べた。各アミノ酸のビールへの添加量は、複数のビール中の各アミノ酸の含有量を測定し、得られた測定値の最大値と最小値の差分の2倍量又は4倍量とした。表1~3に、ビール中の各アミノ酸の含有量の測定値の最大値と最小値、及びこれらの差分の2倍量と4倍量の結果を示す。
[Reference Example 1]
Each amino acid was added to commercially available beer, and the effect on foam retention was investigated. The amount of each amino acid added to beer was set to 2 times or 4 times the difference between the maximum value and the minimum value of the obtained measured values by measuring the content of each amino acid in a plurality of beers. Tables 1 to 3 show the maximum and minimum values of the measured values of the content of each amino acid in beer, and the results of double and quadruple amounts of these differences.

具体的には、市販のビールに、大瓶(633mL)1本あたりに各アミノ酸を表1に記載の2種類の添加量(差分の2倍量又は4倍量)を添加し、再打栓した。この大瓶を10回転撹拌した後、4℃で一晩保存した後、NIBEM値を測定した(n=2)。測定結果を表1~3に示す。表中、「NIBEM値(秒)」欄の「無添加」は、アミノ酸を添加していないビールの測定結果を示す。 Specifically, to commercially available beer, each amino acid was added to each large bottle (633 mL) in the two types of addition amounts shown in Table 1 (double or four times the difference), and the beer was re-plugged. .. The large bottle was stirred 10 times, stored overnight at 4 ° C., and then the NIBEM value was measured (n = 2). The measurement results are shown in Tables 1 to 3. In the table, "no addition" in the "NIBEM value (seconds)" column indicates the measurement result of beer to which no amino acid is added.

Figure 0007049821000001
Figure 0007049821000001

Figure 0007049821000002
Figure 0007049821000002

Figure 0007049821000003
Figure 0007049821000003

この結果、アルギニン、リジン、ヒスチジン、グルタミン酸、グルタミン、グリシン、イソロイシン、プロリン、又はGABAを添加したビールでは、無添加のものよりもNIBEM値が小さくなっており、泡持ちが悪化していた。これらの結果から、アルギニン、リジン、ヒスチジン、グルタミン酸、グルタミン、グリシン、イソロイシン、プロリン、及びGABAが泡持ちに影響を与えるアミノ酸であり、これらの含有量を低減させることでビール様発酵麦芽飲料の泡持ちが向上することが示唆された。 As a result, the beer to which arginine, lysine, histidine, glutamic acid, glutamine, glycine, isoleucine, proline, or GABA was added had a smaller NIBEM value than that without the addition, and the foam retention was deteriorated. From these results, arginine, lysine, histidine, glutamic acid, glutamine, glycine, isoleucine, proline, and GABA are amino acids that affect foam retention, and by reducing their content, foam of beer-like fermented malt beverages. It was suggested that the holding time would improve.

[比較例1-1~1-3]
麦芽30kgの粉砕物を、50℃、90Lの湯と混合し、得られた混合物を、50℃で60分間保持し、タンパク質分解処理を行った。タンパク質分解処理後の混合物に、別途液化させておいたコーンスターチ10kgと混合した後、得られた混合物を、62℃、30分間保持して糖化させ、麦汁を得た(麦芽比率75質量%)。得られた麦汁を濾過した濾液は、ホップ100gを添加した後、乳酸によりpHを5.2に調整した。pH調整後の麦汁を110分間煮沸した。煮沸後の麦汁(180L)は、ワールプールに40分静置し、トルーブと上澄みを分離した。その後、上澄みをプレート式熱交換器にて約7℃にまで冷却した後、15×10個/mLの下面発酵酵母(Weihenstephan 34株)を接種させ、10℃で10日間発酵させた。その後、発酵液を貯酒槽へ移し、10日間熟成させ、さらに0℃に冷却して10日間安定化させた後、珪藻土濾過を実施し、製品ビールを得た。
[Comparative Examples 1-1 to 1-3]
A pulverized product of 30 kg of malt was mixed with hot water at 50 ° C. and 90 L, and the obtained mixture was held at 50 ° C. for 60 minutes for proteolysis. The mixture after the proteolysis treatment was mixed with 10 kg of cornstarch separately liquefied, and then the obtained mixture was held at 62 ° C. for 30 minutes for saccharification to obtain wort (malt ratio 75% by mass). .. The pH of the filtered filtrate of the obtained wort was adjusted to 5.2 with lactic acid after adding 100 g of hops. The pH-adjusted wort was boiled for 110 minutes. The boiled wort (180 L) was allowed to stand in a whirlpool for 40 minutes to separate the trove and the supernatant. Then, the supernatant was cooled to about 7 ° C. with a plate heat exchanger, and then inoculated with 15 × 10 6 pieces / mL bottom fermenting yeast (Weihenstephan 34 strain) and fermented at 10 ° C. for 10 days. Then, the fermented liquid was transferred to a liquor tank, aged for 10 days, further cooled to 0 ° C. and stabilized for 10 days, and then filtered through diatomaceous earth to obtain a product beer.

得られた製品ビールを壜詰し、このうち3本を比較例1-1、1-2、1-3として、それぞれのNIBEM値、総タンパク質量(mg/L)、塩基性アミノ酸(アルギニン、リジン、ヒスチジン)の合計量(mg/100mL)、及び塩基性アミノ酸以外の6種の泡影響アミノ酸(グルタミン酸、グルタミン、グリシン、イソロイシン、プロリン、及びGABA)の合計量(mg/100mL)を測定した。結果を表4に示す。 The obtained product beer was bottled, and three of them were used as Comparative Examples 1-1, 1-2, and 1-3, and each NIBEM value, total protein amount (mg / L), and basic amino acid (arginine, lysine) were used. , Histidine) and the total amount (mg / 100 mL) of 6 foam-affecting amino acids (glutamic acid, glutamine, glycine, isoleucine, proline, and GABA) other than basic amino acids were measured. The results are shown in Table 4.

[実施例1-1~1-3]
麦芽30kgの粉砕物を、55℃、90Lの湯と混合し、得られた混合物を、55℃で40分間保持し、タンパク質分解処理を行った。タンパク質分解処理後の混合物に、別途液化させておいたコーンスターチ10kgと混合した後、得られた混合物を、62℃、30分間保持して糖化させ、麦汁を得た(麦芽比率75質量%)。得られた麦汁を濾過した濾液は、ホップ100gを添加した後、乳酸によりpHを5.4に調整した。pH調整後の麦汁を70分間煮沸した。煮沸後の麦汁(180L)は、ワールプールに40分静置し、トルーブと上澄みを分離した。その後、上澄みをプレート式熱交換器にて約7℃にまで冷却した後、30×10個/mLの下面発酵酵母(Weihenstephan 34株)を接種させ、12℃で7日間発酵させた。発酵中は、1回/日の頻度で、発酵槽の底に沈降した酵母を引き抜く作業を実施した。その後、発酵液を貯酒槽へ移し、7日間熟成させ、さらに0℃に冷却して3日間安定化させた後、珪藻土濾過を実施し、製品ビールを得た。
[Examples 1-1 to 1-3]
A pulverized product of 30 kg of malt was mixed with hot water at 55 ° C. and 90 L, and the obtained mixture was held at 55 ° C. for 40 minutes for proteolysis. The mixture after the proteolysis treatment was mixed with 10 kg of cornstarch separately liquefied, and then the obtained mixture was held at 62 ° C. for 30 minutes for saccharification to obtain wort (malt ratio 75% by mass). .. The pH of the filtered filtrate of the obtained wort was adjusted to 5.4 with lactic acid after adding 100 g of hops. The pH-adjusted wort was boiled for 70 minutes. The boiled wort (180 L) was allowed to stand in a whirlpool for 40 minutes to separate the trove and the supernatant. Then, the supernatant was cooled to about 7 ° C. with a plate heat exchanger, then inoculated with 30 × 10 6 / mL bottom fermenting yeast (Weihenstephan 34 strains) and fermented at 12 ° C. for 7 days. During fermentation, the work of extracting the yeast that had settled at the bottom of the fermenter was carried out once a day. Then, the fermented liquid was transferred to a liquor tank, aged for 7 days, further cooled to 0 ° C. and stabilized for 3 days, and then filtered through diatomaceous earth to obtain a product beer.

得られた製品ビールを壜詰し、このうち3本を実施例1-1、1-2、1-3として、それぞれのNIBEM値、総タンパク質量(mg/L)、塩基性アミノ酸(アルギニン、リジン、ヒスチジン)の合計量(mg/100mL)、及び塩基性アミノ酸以外の6種の泡影響アミノ酸(グルタミン酸、グルタミン、グリシン、イソロイシン、プロリン、及びGABA)の合計量(mg/100mL)を測定した。結果を表4に示す。 The obtained product beer was bottled, and three of them were used as Examples 1-1, 1-2, and 1-3, and each NIBEM value, total protein amount (mg / L), and basic amino acid (arginine, lysine) were used. , Histidine) and the total amount (mg / 100 mL) of 6 foam-affecting amino acids (glutamic acid, glutamine, glycine, isoleucine, proline, and GABA) other than basic amino acids were measured. The results are shown in Table 4.

Figure 0007049821000004
Figure 0007049821000004

この結果、実施例1-1~1-3では、比較例1-1~1-3よりも、総タンパク質濃度が高く、かつ塩基性アミノ酸や泡影響アミノ酸の合計含有量が少なかった。さらに、実施例1-1~1-3は、比較例1-1~1-3よりも、同じ発酵原料を用いているにもかかわらず、NIBEM値が10秒以上も大きく、泡持ちが向上していた。すなわち、本実施例により、発酵原料に対する麦芽比率が75質量%と高い場合でも、NIBEM値が260~280秒であり、良好な泡持ちのビール様発酵麦芽飲料が製造できた。 As a result, in Examples 1-1 to 1-3, the total protein concentration was higher and the total content of basic amino acids and foam-affecting amino acids was smaller than that of Comparative Examples 1-1 to 1-3. Further, in Examples 1-1 to 1-3, the NIBEM value is larger than that of Comparative Examples 1-1 to 1-3 by 10 seconds or more even though the same fermentation raw material is used, and the foam retention is improved. Was. That is, according to this example, even when the malt ratio to the fermentation raw material was as high as 75% by mass, the NIBEM value was 260 to 280 seconds, and a beer-like fermented malt beverage having good foaming could be produced.

Claims (5)

麦芽を含む発酵原料と原料水とを含む混合物を50℃超、60℃以下で30分間~90分間保持してタンパク質を分解させた後、60℃超90℃未満で糖化処理した後、得られた糖液を煮沸処理し、発酵原料液を調製する仕込工程と、
前記仕込工程で調製された発酵原料液に下面発酵酵母を接種して、発酵槽中で9℃超、12℃以下で発酵を行う発酵工程と、
発酵工程により得られた発酵液を、貯酒槽中で3~7日間熟成させる熟成工程と、
を有し、
前記煮沸処理の煮沸時間が30分間以上100分間未満であり、
前記糖液のpHが5.3~5.8であり、
前記発酵工程から前記熟成工程が終了するまでに、前記発酵槽又は前記貯酒槽の底に沈降した酵母を、少なくとも1回は除去し、
製造されたビール様発酵麦芽飲料のPierce 660 nm Protein Assayにより測定されるタンパク質濃度が150~180mg/Lであり、かつグルタミン、グルタミン酸、グリシン、イソロイシン、γ-アミノ酪酸、及びプロリンの合計含有量が34mg/100mL以下となるように調整することを特徴とする、ビール様発酵麦芽飲料の製造方法。
Obtained after holding a mixture containing a fermentation raw material containing malt and raw water at 50 ° C. or lower for 30 to 90 minutes to decompose the protein, and then saccharifying the mixture at 60 ° C. or lower and lower than 90 ° C. The preparation process of boiling the sugar solution to prepare the fermentation raw material solution,
A fermentation step in which bottom-fermenting yeast is inoculated into the fermentation raw material liquid prepared in the above-mentioned preparation step and fermentation is performed in a fermenter at a temperature of more than 9 ° C and less than 12 ° C.
A aging process in which the fermented liquid obtained in the fermentation process is aged in a liquor tank for 3 to 7 days.
Have,
The boiling time of the boiling treatment is 30 minutes or more and less than 100 minutes.
The pH of the sugar solution is 5.3 to 5.8, and the pH is 5.3 to 5.8.
From the fermentation step to the end of the aging step, the yeast that has settled in the bottom of the fermentation tank or the liquor storage tank is removed at least once.
The produced beer-like fermented malt beverage has a protein concentration of 150-180 mg / L as measured by the Pierce 660 nm Protein Assay and a total content of glutamine, glutamic acid, glycine, isoleucine, γ-aminobutyric acid, and proline. A method for producing a beer-like fermented malt beverage, which comprises adjusting the content to 34 mg / 100 mL or less .
前記発酵原料の全量に対する麦芽の比率が50質量%以上である、請求項1に記載のビール様発酵麦芽飲料の製造方法。 The method for producing a beer-like fermented malt beverage according to claim 1, wherein the ratio of malt to the total amount of the fermented raw material is 50% by mass or more. 製造されたビール様発酵麦芽飲料のアルギニン、リジン、及びヒスチジンの合計含有量が2.0mg/100mL以下となるように調整する、請求項1又は2に記載のビール様発酵麦芽飲料の製造方法。 The method for producing a beer-like fermented malt beverage according to claim 1 or 2 , wherein the total content of arginine, lysine, and histidine of the produced beer-like fermented malt beverage is adjusted to 2.0 mg / 100 mL or less. 製造されたビール様発酵麦芽飲料のNIBEM値が260秒以上となるように調整する、請求項1~のいずれか一項に記載のビール様発酵麦芽飲料の製造方法。 The method for producing a beer-like fermented malt beverage according to any one of claims 1 to 3 , wherein the NIBEM value of the produced beer-like fermented malt beverage is adjusted to be 260 seconds or longer. 発酵原料の全量に対する麦芽の比率が50質量%以上であり、発酵工程を経て製造されるビール様発酵麦芽飲料の泡持ちを向上させる方法であって、
ビール様発酵麦芽飲料中のPierce 660 nm Protein Assayにより測定されるタンパク質濃度を150~180mg/Lとし、グルタミン、グルタミン酸、グリシン、イソロイシン、γ-アミノ酪酸、及びプロリンの合計含有量を34mg/100mL以下に調整することを特徴とする、ビール様発酵麦芽飲料の泡持ち向上方法。
The ratio of malt to the total amount of fermentation raw material is 50% by mass or more, and it is a method for improving the foam retention of beer-like fermented malt beverage produced through the fermentation process.
The protein concentration measured by the Pierce 660 nm Protein Assay in the beer-like fermented malt beverage is 150 to 180 mg / L, and the total content of glutamine, glutamic acid, glycine, isoleucine, γ-aminobutyric acid, and proline is 34 mg / 100 mL or less. A method for improving the foam retention of beer-like fermented malt beverages, which is characterized by adjusting to.
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