JP6930879B2 - Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages - Google Patents

Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages Download PDF

Info

Publication number
JP6930879B2
JP6930879B2 JP2017168928A JP2017168928A JP6930879B2 JP 6930879 B2 JP6930879 B2 JP 6930879B2 JP 2017168928 A JP2017168928 A JP 2017168928A JP 2017168928 A JP2017168928 A JP 2017168928A JP 6930879 B2 JP6930879 B2 JP 6930879B2
Authority
JP
Japan
Prior art keywords
fermentation
2m3mb
reducing
fermented beer
raw material
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.)
Active
Application number
JP2017168928A
Other languages
Japanese (ja)
Other versions
JP2019041688A (en
Inventor
重都 野場
重都 野場
奈々 八子
奈々 八子
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.)
Asahi Breweries Ltd
Original Assignee
Asahi Breweries 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 Asahi Breweries Ltd filed Critical Asahi Breweries Ltd
Priority to JP2017168928A priority Critical patent/JP6930879B2/en
Priority to PCT/JP2018/025363 priority patent/WO2019044163A1/en
Publication of JP2019041688A publication Critical patent/JP2019041688A/en
Application granted granted Critical
Publication of JP6930879B2 publication Critical patent/JP6930879B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C5/00Other raw materials for the preparation of beer
    • C12C5/02Additives for beer
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12GWINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
    • C12G3/00Preparation of other alcoholic beverages
    • C12G3/04Preparation of other alcoholic beverages by mixing, e.g. for preparation of liqueurs

Description

本発明は、ビール様発泡性飲料において、オフフレーバーの1種であるタマネギ様臭の発生を抑制する方法に関する。 The present invention relates to a method for suppressing the generation of an onion-like odor, which is a kind of off-flavour, in a beer-like sparkling beverage.

ビールや発泡酒等の発酵ビール様発泡性飲料においては、コゲ臭・日光臭様臭やタマネギ様臭等のオフフレーバーが認められる場合があり、発酵ビール様発泡性飲料の品質向上のためには、これらのオフフレーバーの制御が重要である。原因物質やその生成機序が解明できれば、オフフレーバーを効率よく制御できることが期待できる。しかしながら、オフフレーバーの原因物質は様々であり、その生成機序の解明も困難である。例えば、ビール中のタマネギ様臭の原因物質が2−メルカプト−3−メチル−1−ブタノール(2-mercapto-3-methyl-1-butanol,2M3MB)であることは知られているが(例えば、非特許文献1参照。)、どのような作用機序により2M3MBが生成されるのかは未だ解明されていない。 In fermented beer-like sparkling beverages such as beer and low-malt beer, off-flavors such as kogation odor, sunlight odor, and onion-like odor may be observed, and in order to improve the quality of fermented beer-like sparkling beverages. , Control of these off-flavors is important. If the causative substance and its generation mechanism can be elucidated, it can be expected that off-flavour can be controlled efficiently. However, the causative substances of off-flavour are various, and it is difficult to elucidate the mechanism of their formation. For example, it is known that the causative agent of onion-like odor in beer is 2-mercapto-3-methyl-1-butanol (2M3MB) (for example, 2M3MB). (Refer to Non-Patent Document 1), it has not yet been clarified by what mechanism of action 2M3MB is produced.

一方で、アミノ酸は発酵における重要な窒素源である。例えば、アミノ酸は酵母が増殖するために欠かせない栄養素であり、不足すると酵母の代謝機能に異常が生じ、オフフレーバーの1種である発酵不順臭が発生しやすくなる。また、ビールの主要な香気成分である高級アルコール及びエステルの多くは、発酵工程におけるアミノ酸代謝により生成される。このため、発酵不順の防止や香味調整のために、酵母添加前の麦汁や発酵完了前の発酵液に、アミノ酸を添加する方法がある(特許文献1及び2参照。)。 On the other hand, amino acids are an important source of nitrogen in fermentation. For example, amino acids are nutrients that are indispensable for the growth of yeast, and if they are deficient, abnormalities occur in the metabolic function of yeast, and an unseasonable fermentation odor, which is a kind of off-flavour, is likely to occur. In addition, most of the higher alcohols and esters, which are the main aroma components of beer, are produced by amino acid metabolism in the fermentation process. Therefore, in order to prevent irregular fermentation and adjust the flavor, there is a method of adding amino acids to wort before yeast addition and fermentation broth before completion of fermentation (see Patent Documents 1 and 2).

特開2015−116125号公報Japanese Unexamined Patent Publication No. 2015-116125 特開2015−116126号公報Japanese Unexamined Patent Publication No. 2015-116126

Olsen et al., Carlsberg Research Communication, 1988, vol.53, p.1-9.Olsen et al., Carlsberg Research Communication, 1988, vol.53, p.1-9. Iijima et al.,Journal of Applied Microbiology,2010,vol.109, p.1906-1913.Iijima et al., Journal of Applied Microbiology, 2010, vol.109, p.1906-1913.

本発明は、発酵ビール様発泡性飲料に対して、タマネギ様臭の主な原因物質である2M3MBの含有量を低減させる方法を提供することを目的とする。 An object of the present invention is to provide a method for reducing the content of 2M3MB, which is a main causative substance of an onion-like odor, in a fermented beer-like effervescent beverage.

本発明者は、上記課題を解決すべく鋭意研究した結果、酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に特定のアミノ酸を添加することによって、発酵中の2M3MBの生成が抑制され、製造された発酵ビール様発泡性飲料の2M3MBの含有量を低減できることを見出し、本発明を完成させた。 As a result of diligent research to solve the above problems, the present inventor has produced 2M3MB during fermentation by adding a specific amino acid to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. The present invention has been completed by finding that the content of 2M3MB of a fermented beer-like effervescent beverage produced that is suppressed can be reduced.

本発明に係る発酵ビール様発泡性飲料の2M3MBの含有量を低減する方法は、下記[1]〜[6]である。
[1] 発酵工程を経て製造される発酵ビール様発泡性飲料の2M3MBの含有量を低減する方法であって、
酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、バリン、ヒスチジン、及びアラニンからなる群より選択される1種以上のアミノ酸を添加することを特徴とする、発酵ビール様発泡性飲料の2M3MBの低減方法。
[2] 発酵工程を経て製造される発酵ビール様発泡性飲料の2M3MBの含有量を低減する方法であって、
酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、アスパラギン、アスパラギン酸、グルタミン、グルタミン酸、バリン、ヒスチジン、及びアラニンからなる群より選択される1種以上のアミノ酸を添加することを特徴とする、発酵ビール様発泡性飲料の2M3MBの低減方法。
[3] 発酵工程を経て製造される発酵ビール様発泡性飲料の2M3MBの含有量を低減する方法であって、
酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、フェニルアラニン、システイン、メチオニン、セリン、ロイシン、及びチロシンからなる群より選択される1種以上のアミノ酸を添加することを特徴とする、発酵ビール様発泡性飲料の2M3MBの低減方法。
[4] 前記アミノ酸の総添加量が、前記発酵原料液又は前記発酵液1L当たり0.2g以上である、前記[1]〜[3]のいずれかの発酵ビール様発泡性飲料の2M3MBの低減方法。
[5] 前記アミノ酸の総添加量が、前記発酵原料液又は前記発酵液1L当たり0.2〜1.0gである、前記[1]〜[3]のいずれかの発酵ビール様発泡性飲料の2M3MBの低減方法。
[6] 前記発酵ビール様発泡性飲料の2M3MBの含有量を、0.5ppb以下に低減する、前記[1]〜[3]のいずれかの発酵ビール様発泡性飲料の2M3MBの低減方法。
The methods for reducing the content of 2M3MB in the fermented beer-like sparkling beverage according to the present invention are as follows [1] to [6].
[1] A method for reducing the content of 2M3MB in a fermented beer-like sparkling beverage produced through a fermentation step.
Fermented beer-like foaming characterized by adding one or more amino acids selected from the group consisting of valine, histidine, and alanine to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. A method for reducing 2M3MB of sex beverages.
[2] A method for reducing the content of 2M3MB in a fermented beer-like sparkling beverage produced through a fermentation step.
To add one or more amino acids selected from the group consisting of aspartic acid, aspartic acid, glutamine, glutamic acid, valine, histidine, and alanine to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. A method for reducing 2M3MB of a fermented beer-like effervescent beverage, which comprises.
[3] A method for reducing the content of 2M3MB in a fermented beer-like sparkling beverage produced through a fermentation step.
It is characterized by adding one or more amino acids selected from the group consisting of phenylalanine, cysteine, methionine, serine, leucine, and tyrosine to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. A method for reducing 2M3MB of fermented beer-like effervescent beverages.
[4] Reduction of 2M3MB of the fermented beer-like effervescent beverage according to any one of [1] to [3], wherein the total amount of the amino acids added is 0.2 g or more per 1 L of the fermented raw material liquid or the fermented liquid. Method.
[5] The fermented beer-like effervescent beverage according to any one of [1] to [3], wherein the total amount of the amino acids added is 0.2 to 1.0 g per 1 L of the fermented raw material liquid or the fermented liquid. 2M3MB reduction method.
[6] The method for reducing 2M3MB of a fermented beer-like sparkling beverage according to any one of the above [1] to [3], which reduces the content of 2M3MB of the fermented beer-like sparkling beverage to 0.5 ppb or less.

本発明に係る発酵ビール様発泡性飲料の2M3MBの低減方法により、発酵工程における2M3MBの生成を抑制することができ、タマネギ様臭が抑制された発酵ビール様発泡性飲料が製造できる。 According to the method for reducing 2M3MB of a fermented beer-like effervescent beverage according to the present invention, the production of 2M3MB in the fermentation step can be suppressed, and a fermented beer-like effervescent beverage having an suppressed onion-like odor can be produced.

実施例2において、アスパラギン酸、バリン、又はグルタミン酸を添加した試験用麦汁(麦芽使用比率25質量%)から得られた発酵液の2M3MB濃度の測定結果を示した図である。In Example 2, it is a figure which showed the measurement result of the 2M3MB concentration of the fermented liquid obtained from the test wort (malt use ratio 25% by mass) to which aspartic acid, valine, or glutamic acid was added.

本発明及び本願明細書において、「発酵ビール様発泡性飲料」とは、発酵工程を経て製造された飲料であって、アルコール含有量や麦芽の使用の有無に関わらず、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、発酵ビール様発泡性飲料は、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。また、麦芽を原料とする飲料であってもよく、麦芽を原料としない飲料であってもよい。発酵ビール様発泡性飲料としては、具体的には、ビール、麦芽を原料とする発泡酒、麦芽を使用しない発泡性アルコール飲料、ローアルコール発泡性飲料、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 specification of the present application, the "fermented beer-like effervescent beverage" is a beverage produced through a fermentation step, and is equivalent to or equivalent to beer regardless of the alcohol content or the use of malt. It means an effervescent beverage having a similar flavor, taste and texture, and having a high feeling of thirst and drinkability. That is, the fermented beer-like effervescent 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. Further, it may be a beverage made from malt or a beverage not made from malt. Specific examples of the fermented beer-like effervescent beverage include beer, effervescent liquor made from malt, effervescent alcoholic beverage not using malt, low alcohol effervescent beverage, non-alcoholic beer and the like. 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 distillation solution is a solution containing alcohol obtained by a distillation operation, and may be, for example, alcohol for raw materials. Distillation of spirits, whiskey, brandy, wokka, lamb, tequila, gin, shochu, etc. Alcohol and the like can be used.

後記参考例に示すように、2M3MBは、ビール等の発酵ビール様発泡性飲料のタマネギ様臭の原因物質であり、2M3MBの含有量依存的にタマネギ様臭が強くなる。2M3MBは、主に発酵中に生成される。このため、発酵時の2M3MB生成量を抑えることによって、2M3MBの含有量が少なく、タマネギ様臭が抑えられた発酵ビール様発泡性飲料を製造できる。 As shown in the reference example below, 2M3MB is a causative substance of the onion-like odor of fermented beer-like effervescent beverages such as beer, and the onion-like odor becomes stronger depending on the content of 2M3MB. 2M3MB is mainly produced during fermentation. Therefore, by suppressing the amount of 2M3MB produced during fermentation, it is possible to produce a fermented beer-like sparkling beverage having a low content of 2M3MB and a suppressed onion-like odor.

本発明に係る発酵ビール様発泡性飲料の2M3MBの低減方法(以下、「本発明に係る低減方法」ということがある。)は、発酵工程を経て製造される発酵ビール様発泡性飲料の2M3MBの含有量を低減する方法であって、酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、特定の種類のアミノ酸からなる群より選択される1種以上のアミノ酸を添加することを特徴とする。発酵時の2M3MBの生成は、アミノ酸の影響を強く受ける。発酵時に、特定のアミノ酸を充分量存在させることにより、2M3MBの生成を抑制することができる。 The method for reducing 2M3MB of a fermented beer-like effervescent beverage according to the present invention (hereinafter, may be referred to as “reduction method according to the present invention”) is a method for reducing 2M3MB of a fermented beer-like effervescent beverage produced through a fermentation step. A method for reducing the content, in which one or more amino acids selected from the group consisting of specific types of amino acids are added to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. It is characterized by. The production of 2M3MB during fermentation is strongly influenced by amino acids. The production of 2M3MB can be suppressed by the presence of a sufficient amount of a specific amino acid during fermentation.

発酵時の2M3MBの生成を抑制する効果を有するアミノ酸は、バリン、ヒスチジン、アラニン、アスパラギン、アスパラギン酸、グルタミン、グルタミン酸、フェニルアラニン、システイン、メチオニン、セリン、ロイシン、又はチロシンである。以下、これらの2M3MBの生成抑制作用を有するアミノ酸を総称して、「2M3MB低減用アミノ酸」ということがある。本発明に係る低減方法においては、酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、2M3MB低減用アミノ酸を1種類のみ添加してもよく、2種類以上組み合わせて添加してもよい。 Amino acids that have the effect of suppressing the production of 2M3MB during fermentation are valine, histidine, alanine, aspartic acid, aspartic acid, glutamine, glutamic acid, phenylalanine, cysteine, methionine, serine, leucine, or tyrosine. Hereinafter, these amino acids having an inhibitory effect on the production of 2M3MB may be collectively referred to as "amino acid for reducing 2M3MB". In the reduction method according to the present invention, only one type of amino acid for reducing 2M3MB may be added to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step, or two or more types may be added in combination. May be good.

本発明に係る低減方法において発酵原料液等に添加される2M3MB低減用アミノ酸としては、より高い2M3MBの生成抑制効果が得られるため、アスパラギン、アスパラギン酸、グルタミン、グルタミン酸、バリン、ヒスチジン、及びアラニンからなる群より選択される1種以上が好ましく、アスパラギン酸、バリン、グルタミン酸、及びヒスチジンからなる群より選択される1種以上がより好ましく、バリン及びヒスチジンからなる群より選択される1種以上がさらに好ましい。また、発酵時のその他の反応に対する影響が比較的小さいことから、本発明に係る低減方法において発酵原料液等に添加される2M3MB低減用アミノ酸としては、バリン、ヒスチジン、及びアラニンからなる群より選択される1種以上であることも好ましい。 As the amino acid for reducing 2M3MB added to the fermentation raw material solution or the like in the reduction method according to the present invention, a higher effect of suppressing the production of 2M3MB can be obtained. One or more selected from the group consisting of aspartic acid, valine, glutamic acid, and histidine is more preferable, and one or more selected from the group consisting of valine and histidine are further preferable. preferable. In addition, since the effect on other reactions during fermentation is relatively small, the 2M3MB reduction amino acid added to the fermentation raw material solution or the like in the reduction method according to the present invention is selected from the group consisting of valine, histidine, and alanine. It is also preferable that there is at least one type of fermentation.

本発明に係る低減方法において発酵原料液等に添加される2M3MB低減用アミノ酸としては、フェニルアラニン、システイン、メチオニン、セリン、ロイシン、及びチロシンからなる群より選択される1種以上であってもよい。これらのアミノ酸は、バリン等よりも2M3MBの生成抑制作用は弱いものの、発酵原料液等へより多くの量を添加することにより、タマネギ様臭を感じない程度に充分に2M3MBの生成を抑制することができる。 The amino acid for reducing 2M3MB added to the fermentation raw material solution or the like in the reduction method according to the present invention may be one or more selected from the group consisting of phenylalanine, cysteine, methionine, serine, leucine, and tyrosine. Although these amino acids have a weaker effect of suppressing the production of 2M3MB than valine and the like, by adding a larger amount to the fermentation raw material solution and the like, the production of 2M3MB can be sufficiently suppressed to the extent that an onion-like odor is not felt. Can be done.

発酵原料液等に添加される2M3MB低減用アミノ酸の量は特に限定されるものではない。発酵原料液等に添加される2M3MB低減用アミノ酸の量が多くなればなるほど、発酵後に得られる発酵ビール様発泡性飲料の2M3MB含有量はより低減される。発酵原料液等に添加される2M3MB低減用アミノ酸量が少量の場合でも、2M3MB低減用アミノ酸量を添加しなかった場合よりも、2M3MB含有量の少ない発酵ビール様発泡性飲料が得られる。 The amount of 2M3MB-reducing amino acid added to the fermentation raw material solution or the like is not particularly limited. The larger the amount of 2M3MB-reducing amino acid added to the fermentation raw material solution or the like, the more the 2M3MB content of the fermented beer-like effervescent beverage obtained after fermentation is reduced. Even when the amount of 2M3MB-reducing amino acid added to the fermentation raw material liquid or the like is small, a fermented beer-like effervescent beverage having a 2M3MB content lower than that when the 2M3MB-reducing amino acid amount is not added can be obtained.

発酵原料液等に添加される2M3MB低減用アミノ酸の量は、最終的に得られる発酵ビール様発泡性飲料の2M3MB含有量が0.5ppb以下となる量であることが好ましく、0.4ppb以下となる量であることがより好ましく、0.1ppb以下となる量であることがさらに好ましく、0ppb(検出限界値未満)となる量であることがよりさらに好ましい。なお、発酵ビール様発泡性飲料の2M3MB濃度は、Iijimaらの方法(非特許文献2)に準じて測定することができる。 The amount of the amino acid for reducing 2M3MB added to the fermentation raw material solution or the like is preferably an amount such that the 2M3MB content of the finally obtained fermented beer-like effervescent beverage is 0.5 ppb or less, preferably 0.4 ppb or less. It is more preferable that the amount is 0.1 ppb or less, and even more preferably 0 ppb (less than the detection limit value). The 2M3MB concentration of the fermented beer-like sparkling beverage can be measured according to the method of Iijima et al. (Non-Patent Document 2).

最終的に得られる発酵ビール様発泡性飲料の2M3MB含有量を所定の濃度以下にするために必要な2M3MB低減用アミノ酸の量は、添加する2M3MB低減用アミノ酸の種類や、使用する酵母の種類、発酵条件、発酵原料液の成分組成等を考慮して適宜調整することができる。例えば、発酵原料液等への2M3MB低減用アミノ酸の総添加量を、発酵原料液又は発酵液の1L当たり1.0g以上とすることにより、充分な2M3MB低減効果が得られ、タマネギ様臭が抑えられた発酵ビール様発泡性飲料が得られる。特に2M3MBの生成抑制作用が強い、アスパラギン、アスパラギン酸、グルタミン、グルタミン酸、バリン、ヒスチジン、及びアラニンからなる群より選択される1種以上を用いる場合には、これらのアミノ酸の総添加量が、発酵原料液又は発酵液の1L当たり0.2〜1.0gとした場合でも、充分な2M3MB低減効果が得られる。 The amount of 2M3MB-reducing amino acid required to reduce the 2M3MB content of the finally obtained fermented beer-like effervescent beverage to a predetermined concentration or less depends on the type of 2M3MB-reducing amino acid to be added, the type of yeast to be used, and the like. It can be appropriately adjusted in consideration of the fermentation conditions, the component composition of the fermentation raw material solution, and the like. For example, by setting the total amount of amino acids for reducing 2M3MB to the fermentation raw material liquid or the like to 1.0 g or more per 1L of the fermentation raw material liquid or the fermentation liquid, a sufficient 2M3MB reduction effect can be obtained and the onion-like odor can be suppressed. The fermented beer-like effervescent beverage is obtained. In particular, when one or more selected from the group consisting of asparagine, aspartic acid, glutamine, glutamic acid, valine, histidine, and alanine, which have a strong inhibitory effect on the production of 2M3MB, is used, the total amount of these amino acids added is fermentation. A sufficient 2M3MB reduction effect can be obtained even when the amount is 0.2 to 1.0 g per 1 L of the raw material solution or the fermented solution.

本発明に係る低減方法を、発酵ビール様発泡性飲料の製造の過程で行うことにより、2M3MB含有量が少なく、タマネギ様臭が抑えられた発酵ビール様発泡性飲料が製造できる。本発明に係る低減方法が適用される発酵ビール様発泡性飲料の製造方法は、特に限定されるものではない。以下、一般的な発酵ビール様発泡性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。一般的な発酵ビール様発泡性飲料は、仕込(発酵原料液調製)、発酵、貯酒、濾過の工程で製造することができる。 By carrying out the reduction method according to the present invention in the process of producing a fermented beer-like effervescent beverage, a fermented beer-like effervescent beverage having a low 2M3MB content and suppressed onion-like odor can be produced. The method for producing a fermented beer-like sparkling beverage to which the reduction method according to the present invention is applied is not particularly limited. Hereinafter, a method in which the reduction method according to the present invention is applied to a general method for producing a fermented beer-like sparkling beverage will be described. A general fermented beer-like effervescent beverage can be produced by a process of preparation (preparation of fermented raw material liquid), fermentation, storage of sake, and filtration.

まず、仕込工程(発酵原料液調製工程)として、穀物原料及び糖質原料からなる群より選択される1種以上から発酵原料液を調製する。具体的には、まず、穀物原料と糖質原料の少なくともいずれかと原料水とを含む混合物を調製して加温し、穀物原料等の澱粉質を糖化させる。糖液の原料としては、穀物原料のみを用いてもよく、糖質原料のみを用いてもよく、両者を混合して用いてもよい。 First, as a preparation step (fermentation raw material liquid preparation step), a fermentation raw material liquid is prepared from one or more selected from the group consisting of grain raw materials and sugar raw materials. Specifically, first, a mixture containing at least one of a grain raw material and a sugar raw material and raw material water is prepared and heated to saccharify starch such as a grain raw material. As the raw material of the sugar solution, only the grain raw material may be used, only the sugar raw material may be used, or both may be mixed and used.

穀物原料としては、例えば、大麦や小麦、これらの麦芽等の麦類、米、トウモロコシ、大豆等の豆類、イモ類等が挙げられる。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。穀物類の粉砕処理は、常法により行うことができる。穀物粉砕物としては、麦芽粉砕物、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。本発明においては、用いられる穀物粉砕物は、麦芽粉砕物であることが好ましい。麦芽粉砕物を用いることにより、ビールらしさがよりはっきりとした発酵ビール様発泡性飲料を製造することができる。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、所定の粒度に粉砕したものであればよい。また、本発明において用いられる穀物原料としては、1種類の穀物原料であってもよく、複数種類の穀物原料を混合したものであってもよい。例えば、主原料として麦芽粉砕物を、副原料として米やトウモロコシの粉砕物を用いてもよい。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 the grain raw material include barley and wheat, wheat such as malt thereof, beans such as rice, corn and soybean, and potatoes. The grain raw material can be used as a grain syrup, a grain extract, or the like, but is preferably used as a crushed grain product obtained by crushing. The crushing treatment of grains can be carried out by a conventional method. The crushed grain may be a crushed malt, cornstarch, corn grits, or the like, which has been subjected to a treatment usually performed before and after the crushing treatment. In the present invention, the crushed grain product used is preferably a crushed malt product. By using the crushed malt product, it is possible to produce a fermented beer-like effervescent beverage having a clearer beer-like character. The crushed malt product may be any crushed barley, for example, Nijo barley, which is germinated by a conventional method, dried, and then crushed to a predetermined particle size. Further, the grain raw material used in the present invention may be one kind of grain raw material or a mixture of a plurality of kinds of grain raw materials. For example, crushed malt may be used as the main raw material, and crushed rice or corn may be used as the auxiliary raw material. Examples of the sugar raw material include sugars such as liquid sugar.

発酵原料の種類や組成にかかわらず、発酵時に2M3MB低減用アミノ酸を添加することにより、得られる発酵ビール様発泡性飲料の2M3MB含有量を低減させることができる。このため、本発明に係る低減方法は、麦芽使用比率(発酵原料全体に占める麦芽の使用量の割合)が100質量%の発酵ビール様発泡性飲料の製造方法に適用してもよく、麦芽使用比率が0質量%超100質量%未満の発酵ビール様発泡性飲料の製造方法に適用してもよく、発酵原料として麦芽を使用しない発酵ビール様発泡性飲料の製造方法に適用してもよい。 Regardless of the type and composition of the fermentation raw material, the 2M3MB content of the obtained fermented beer-like sparkling beverage can be reduced by adding the amino acid for reducing 2M3MB at the time of fermentation. Therefore, the reduction method according to the present invention may be applied to a method for producing a fermented beer-like effervescent beverage in which the malt usage ratio (the ratio of the amount of malt used to the total fermentation raw material) is 100% by mass, and malt is used. It may be applied to a method for producing a fermented beer-like effervescent beverage having a ratio of more than 0% by mass and less than 100% by mass, or may be applied to a method for producing a fermented beer-like effervescent beverage that does not use malt as a fermentation raw material.

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、ホップ、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 raw materials may be added to the mixture containing the fermentation raw material and the raw material water. Examples of the auxiliary raw material include hops, dietary fiber, yeast extract, fruit juice, bitterness, coloring agents, fragrances, and fragrances. Further, if necessary, a saccharifying enzyme such as α-amylase, glucoamylase and pullulanase, and an enzyme agent such as protease can be added.

糖化処理は、穀物原料等由来の酵素や、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、用いた穀物原料等の種類、発酵原料全体に占める穀物原料の割合、添加した酵素の種類や混合物の量、目的とする発酵ビール様発泡性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、穀物原料等を含む混合物を35〜70℃で20〜90分間保持する等、常法により行うことができる。 The saccharification treatment is carried out using an enzyme derived from a grain raw material or the like or an enzyme added separately. The temperature and time during the saccharification process are determined by the type of grain raw material used, the ratio of the grain raw material to the total fermentation raw material, the type and amount of the added enzyme, the quality of the target fermented beer-like effervescent beverage, etc. It will be adjusted as appropriate in consideration. For example, the saccharification treatment can be carried out by a conventional method, such as holding a mixture containing a grain raw material or the like at 35 to 70 ° C. for 20 to 90 minutes.

糖化処理後に得られた糖液を煮沸することにより、煮汁(糖液の煮沸物)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。煮沸方法及びその条件は、適宜決定することができる。 By boiling the sugar solution obtained after the saccharification treatment, a broth (boiled product of the sugar solution) can be prepared. 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 this may be boiled. The boiling method and its conditions can be appropriately determined.

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発酵ビール様発泡性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)及び煮沸条件は、適宜決定することができる。 A fermented beer-like effervescent beverage having a desired flavor can be produced by appropriately adding flavors and the like before or during the boiling treatment. In particular, hops are preferably added before or during the boiling treatment. 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 boiling conditions can be appropriately determined.

仕込工程後、発酵工程前に、調製された煮汁から、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。この際の煮汁の温度は、15℃以上であればよく、一般的には50〜80℃程度で行われる。粕を除去した後の煮汁(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。この粕を除去した後の煮汁が、発酵原料液となる。 After the preparation step and before the fermentation step, it is preferable to remove the meals such as proteins generated by the precipitation from the prepared broth. The lees may be removed by any solid-liquid separation treatment, but in general, the precipitate is removed using a tank called a whirlpool. The temperature of the broth at this time may be 15 ° C. or higher, and is generally about 50 to 80 ° C. After removing the lees, the broth (filtrate) is cooled to an appropriate fermentation temperature with a plate cooler or the like. The broth after removing the lees becomes the fermentation raw material liquid.

次いで、発酵工程として、冷却した発酵原料液に酵母を接種して、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。上面発酵酵母であってもよく、下面発酵酵母であってもよいが、大型醸造設備への適用が容易であることから、下面発酵酵母であることが好ましい。発酵温度は特に限定されるものではなく、例えば、0〜15℃で行うことができ、4〜12℃で行うことが好ましい。 Next, as a fermentation step, yeast is inoculated into the cooled fermentation raw material liquid to perform fermentation. 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 yeast used for fermentation is not particularly limited, and usually, yeast used for producing alcoholic beverages can be appropriately selected and used. It may be a top-fermenting yeast or a bottom-fermenting yeast, but it is preferably a bottom-fermenting yeast because it can be easily applied to a large-scale brewing facility. The fermentation temperature is not particularly limited, and for example, it can be carried out at 0 to 15 ° C., preferably 4 to 12 ° C.

2M3MB低減用アミノ酸は、発酵時に存在していれば、2M3MB低減効果が得られる。このため、本発明に係る低減方法では、2M3MB低減用アミノ酸を、酵母を接種する前の発酵原料液に添加してもよく、発酵工程中の発酵液に添加してもよい。発酵液に添加する場合、発酵終了時点までの任意の時点で添加することができる。より充分な2M3MB低減効果が得られるため、本発明に係る低減方法では、2M3MB低減用アミノ酸を、発酵工程の比較的初期の段階までに添加することが好ましく、酵母を接種する前の発酵原料液に添加することがより好ましい。 If the amino acid for reducing 2M3MB is present at the time of fermentation, the effect of reducing 2M3MB can be obtained. Therefore, in the reduction method according to the present invention, the amino acid for reducing 2M3MB may be added to the fermentation raw material solution before inoculating yeast, or may be added to the fermentation solution during the fermentation step. When added to the fermentation broth, it can be added at any time until the end of fermentation. In the reduction method according to the present invention, it is preferable to add the amino acid for reducing 2M3MB by a relatively early stage of the fermentation step, because a more sufficient effect of reducing 2M3MB can be obtained. It is more preferable to add to.

発酵工程後、貯酒工程として、得られた発酵液を、貯酒タンク中で熟成させ、0℃程度の低温条件下で貯蔵し安定化させる。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、目的の発酵ビール様発泡性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0.4〜0.5μm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。 After the fermentation step, as a liquor storage step, the obtained fermented liquor is aged in a liquor storage tank and stored and stabilized under a low temperature condition of about 0 ° C. 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 a desired fermented beer-like effervescent beverage. The filtration treatment may be a method capable of removing yeast by filtration, and examples thereof include diatomaceous earth filtration and filter filtration with a filter having an average pore size of about 0.4 to 0.5 μm.

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.

<発酵ビール様発泡性飲料の2M3MB濃度の測定>
以降の実施例等において、発酵ビール様発泡性飲料の2M3MB濃度は、Iijimaらの方法(非特許文献2)に準じて測定した。
<Measurement of 2M3MB concentration of fermented beer-like sparkling beverage>
In the following examples and the like, the 2M3MB concentration of the fermented beer-like effervescent beverage was measured according to the method of Iijima et al. (Non-Patent Document 2).

具体的には、まず、500mLの麦汁に、25mLの2mM p−ヒドロキシ水銀安息香酸(p―HMB)と、500μLのトリスバッファー(0.1M トリス)へ溶解させた20mM tert−ブチル−4−メトキシフェノール(BHA)と、100μLの500mg/mLの4−メトキシ−2−メチル−2−メルカプト−ブタン(4M2M2MB)溶液と、を加えて、密封し、室温で、攪拌子で激しく攪拌し、麦汁中の含硫化合物をp−HMBに結合させた。4M2M2MBは、内部標準物質として添加した。結合した反応物を、Dowex−1(強アニオン交換樹脂)に吸着させた後、0.2mM BHAを含む100mLの0.1M 酢酸バッファー(pH6)を用いて当該樹脂を洗浄した。 Specifically, first, 20 mM tert-butyl-4- dissolved in 25 mL of 2 mM p-hydroxymercury benzoic acid (p-HMB) and 500 μL of tris buffer (0.1 M tris) in 500 mL of wheat juice. Methoxyphenol (BHA) and 100 μL of 500 mg / mL 4-methoxy-2-methyl-2-mercapto-butane (4M2M2MB) solution are added, sealed, stirred vigorously with a stir bar at room temperature and wheat. The sulfur-containing compound in the juice was bound to p-HMB. 4M2M2MB was added as an internal standard. The bound reactant was adsorbed on Dowex-1 (strong anion exchange resin) and then washed with 100 mL of 0.1 M acetate buffer (pH 6) containing 0.2 mM BHA.

次いで、10mg/mLのL−システイン塩酸塩を含む100mLの0.1M 酢酸ナトリウムバッファー(pH6)により、当該樹脂から含硫化合物を溶出させた。得られた溶出液に対して、0.5mLの酢酸エチルと5mLのジクロロメタン溶液を用いて2回溶媒抽出を行い、得られた有機溶媒層を無水硫酸ナトリウムにより脱水した。脱水後の有機溶媒層を室温、窒素気流下で100μLまで濃縮した後、当該有機溶媒層に含まれている含硫化合物をGC/MSにて定量した。 The sulfur-containing compound was then eluted from the resin with 100 mL of 0.1 M sodium acetate buffer (pH 6) containing 10 mg / mL L-cysteine hydrochloride. The obtained eluate was subjected to solvent extraction twice with 0.5 mL of ethyl acetate and 5 mL of dichloromethane solution, and the obtained organic solvent layer was dehydrated with anhydrous sodium sulfate. The dehydrated organic solvent layer was concentrated to 100 μL at room temperature under a nitrogen stream, and then the sulfur-containing compound contained in the organic solvent layer was quantified by GC / MS.

(GC/MS条件)
ガスクロマトグラフ:「Agilent 6890 ガスクロマトグラフ 」(Agilent Technologies社製)
検出器:「MSD5975」(Agilent Technologies社製)
カラム:「DB−WAX capillary column」(長さ:60m、内径:0.25mm、膜厚:0.25μm、Agilent Technologies社製)
注入口温度:250℃
注入モード:パルス化スプリットレスインジェクションモード(pulsed splitless injection mode)
注入量:1μL
キャリアガス:ヘリウム(1mL/分)
カラム温度設定:40℃(5分間保持)−(5℃/分)−160℃(5分間)
イオン化条件:70eV
測定モード:シングルイオン−モニタリングモード(single ion-monitoring(SIM) mode)
定量:2M3MBのピークエリア面積と内部標準品のピークエリア面積との比較にて実施。
(GC / MS conditions)
Gas chromatograph: "Agilent 6890 gas chromatograph" (manufactured by Agilent Technologies)
Detector: "MSD5975" (manufactured by Agilent Technologies)
Column: "DB-WAX capillary volume" (length: 60 m, inner diameter: 0.25 mm, film thickness: 0.25 μm, manufactured by Agilent Technologies)
Injection port temperature: 250 ° C
Injection mode: pulsed splitless injection mode
Injection volume: 1 μL
Carrier gas: Helium (1 mL / min)
Column temperature setting: 40 ° C (hold for 5 minutes)-(5 ° C / min) -160 ° C (5 minutes)
Ionization conditions: 70 eV
Measurement mode: single ion-monitoring (SIM) mode
Quantification: Conducted by comparing the peak area area of 2M3MB with the peak area area of the internal standard product.

<タマネギ様臭の強度の官能評価>
以降の実施例等において、発酵ビール様発泡性飲料のタマネギ様臭の強度は、ブラインドにて、表1に示す評価基準で評価した。官能評価は、各サンプルについてn=3で実施し、評点を平均した値を、当該サンプルのタマネギ様臭強度値とした。
<Sensory evaluation of onion-like odor intensity>
In the following examples and the like, the intensity of the onion-like odor of the fermented beer-like sparkling beverage was evaluated blindly according to the evaluation criteria shown in Table 1. The sensory evaluation was carried out for each sample at n = 3, and the value obtained by averaging the scores was taken as the onion-like odor intensity value of the sample.

Figure 0006930879
Figure 0006930879

[参考例1]
発酵ビール様発泡性飲料の2M3MBの含有量とタマネギ様臭の強度の相関を調べた。具体的には、麦芽使用比率25質量%の市販の発酵ビール様発泡性飲料(市販品A)と麦芽使用比率100質量%の市販の発酵ビール様発泡性飲料(市販品B)に、それぞれ最終濃度が表2の濃度となるように2M3MBを添加し、タマネギ様臭の強度を官能評価した。評価結果を表2に示す。なお、市販品Aの2M3MB濃度は0.06ppbであり、市販品Bの2M3MB濃度は0.13ppbであった。
[Reference example 1]
The correlation between the 2M3MB content of the fermented beer-like sparkling beverage and the intensity of the onion-like odor was investigated. Specifically, the final product is a commercially available fermented beer-like effervescent beverage (commercially available product A) having a malt usage ratio of 25% by mass and a commercially available fermented beer-like effervescent beverage (commercially available product B) having a malt usage ratio of 100% by mass. 2M3MB was added so that the concentration became the concentration shown in Table 2, and the intensity of the onion-like odor was functionally evaluated. The evaluation results are shown in Table 2. The 2M3MB concentration of the commercial product A was 0.06 ppb, and the 2M3MB concentration of the commercial product B was 0.13 ppb.

Figure 0006930879
Figure 0006930879

市販品Aは麦芽使用比率が25質量%であり、市販品Bは麦芽使用比率が100質量%であり、さらにその原料も全く異なる。つまり、市販品Aと市販品Bは、エキス分濃度、香気成分の種類や含有量、呈味成分の種類や含有量等はいずれも異なる。にもかかわらず、表2に示すように、市販品Aと市販品Bでは、2M3MBの最終濃度が同じサンプル同士は、タマネギ様臭の強度もほぼ同程度であった。これらの結果から、発酵ビール様発泡性飲料のタマネギ様臭の強度は、飲料の組成にかかわらず、2M3MBの含有量に依存することが明らかとなった。また、2M3MB濃度が0.1ppbのサンプルの強度値がほぼ1であり、0.2ppbのサンプルの強度値が2.0であったことから、2M3MBの弁別閾は0.1〜0.2ppbの範囲内にあることがわかった。 The commercial product A has a malt usage ratio of 25% by mass, the commercial product B has a malt usage ratio of 100% by mass, and the raw materials thereof are completely different. That is, the commercial product A and the commercial product B are all different in the extract content concentration, the type and content of the aroma component, the type and content of the taste component, and the like. Nevertheless, as shown in Table 2, in the commercial product A and the commercial product B, the samples having the same final concentration of 2M3MB had almost the same intensity of the onion-like odor. From these results, it was clarified that the intensity of the onion-like odor of the fermented beer-like effervescent beverage depends on the content of 2M3MB regardless of the composition of the beverage. Further, since the intensity value of the sample having a 2M3MB concentration of 0.1 ppb was approximately 1, and the intensity value of the sample having a 0.2 ppb concentration was 2.0, the discrimination threshold of 2M3MB was 0.1 to 0.2 ppb. It turned out to be within range.

[実施例1]
発酵ビール様発泡性飲料の製造の際の発酵において、2,3−エポキシ−3−メチルブタナール(2,3-epoxy-3-methyl-butanal,EMBal)が酸素の存在下で酵母によって代謝されることにより、2M3MBが生成される。そこで、2M3MBの原因物質であるEMBalの量を揃えた麦汁を用いて、仕込〜発酵時に添加されたアミノ酸と2M3MBの生成量の関係を調べた。
[Example 1]
During fermentation during the production of fermented beer-like effervescent beverages, 2,3-epoxy-3-methyl-butanal (EMBal) is metabolized by yeast in the presence of oxygen. As a result, 2M3MB is generated. Therefore, the relationship between the amino acids added during the preparation and fermentation and the amount of 2M3MB produced was investigated using wort in which the amount of EMBal, which is the causative substance of 2M3MB, was the same.

麦汁は、以下の通りにして製造した。まず、大麦麦芽3.5gを粉砕し、50℃の湯200mLと混合した。次いで、この混合物を50℃で30分間インキュベートしてタンパク質を分解させたのち、得られたマイシェを65℃、30分間インキュベートして糖化させた。糖化により得られた麦汁を濾過した後、濾過された麦汁に10gのショ糖を添加して濃度調整し、エキス濃度12%の麦汁(発酵原料液)を得た。この麦汁に、EMBalを終濃度が40ppbとなるように添加したものを、試験用麦汁(麦芽使用比率25質量%)とした。 The wort was produced as follows. First, 3.5 g of barley malt was crushed and mixed with 200 mL of hot water at 50 ° C. The mixture was then incubated at 50 ° C. for 30 minutes to degrade the protein, and the resulting maiche was incubated at 65 ° C. for 30 minutes for saccharification. After filtering the wort obtained by saccharification, 10 g of sucrose was added to the filtered wort to adjust the concentration, and a wort (fermentation raw material liquid) having an extract concentration of 12% was obtained. A test wort (malt use ratio 25% by mass) was prepared by adding EMBal to this wort so as to have a final concentration of 40 ppb.

また、濾過された麦汁にショ糖を添加せず、そのままエキス濃度12%の麦汁に調整し、これにEMBalを終濃度が40ppbとなるように添加したものを、試験用麦汁(麦芽使用比率100質量%)とした。 In addition, sucrose was not added to the filtered wort, but the wort was adjusted to an extract concentration of 12% as it was, and EMBal was added to the filtered wort so that the final concentration was 40 ppb. The usage ratio was 100% by mass).

試験用麦汁(麦芽使用比率25質量%)又は試験用麦汁(麦芽使用比率100質量%)に、表3に記載のアミノ酸を終濃度が1mg/mLとなるように添加した後、酵母を20×10個/mLとなるように添加し、12℃で7日間発酵させた。発酵終了後の発酵液を遠心分離処理(7000rpm×15分間)して酵母を除去したもの(発酵ビール様発泡性飲料)について、2M3MB濃度を測定した。測定結果を表3に示す。 The amino acids shown in Table 3 are added to the test wort (malt usage ratio 25% by mass) or the test wort (malt usage ratio 100% by mass) so that the final concentration is 1 mg / mL, and then yeast is added. It was added to 20 × 10 6 pieces / mL and fermented at 12 ° C. for 7 days. The 2M3MB concentration of the fermented liquid after completion of fermentation was measured by centrifuging (7000 rpm × 15 minutes) to remove yeast (fermented beer-like effervescent beverage). The measurement results are shown in Table 3.

Figure 0006930879
Figure 0006930879

アミノ酸を添加しなかった場合、試験用麦汁(麦芽使用比率25質量%)の発酵液の2M3MB濃度は0.8ppbであったのに対して、試験用麦汁(麦芽使用比率100質量%)の発酵液の2M3MB濃度は1.9ppbであり、麦芽使用比率が高いほど発酵中に生成される2M3MBが多くなることがわかった。試験用麦汁(麦芽使用比率25質量%)にバリン、ヒスチジン、アラニン、アスパラギン、アスパラギン酸、グルタミン、グルタミン酸、フェニルアラニン、システイン、メチオニン、セリン、ロイシン、又はチロシンを添加した場合、得られた発酵液の2M3MB濃度は0.5ppb以下であり、これらのアミノ酸を添加して発酵することにより、2M3MBの生成が抑制されることがわかった。一方で、試験用麦汁(麦芽使用比率25質量%)にプロリン、リシン、トリプトファン、又はトレオニンを添加した場合、得られた発酵液の2M3MB濃度はアミノ酸無添加の場合と同程度であり、これらのアミノ酸は2M3MBの生成と関係ないことが示唆された。また、試験用麦汁(麦芽使用比率25質量%)にグリシン、アルギニン、又はイソロイシンを添加した場合、得られた発酵液の2M3MB濃度は1.4ppb以上であり、これらのアミノ酸を添加して発酵することにより、2M3MBの生成が促進されることがわかった。 When no amino acid was added, the 2M3MB concentration of the fermented solution of the test wort (malt use ratio 25% by mass) was 0.8 ppb, whereas the test wort (malt use ratio 100% by mass) was 0.8 ppb. The 2M3MB concentration of the fermented liquid was 1.9 ppb, and it was found that the higher the malt usage ratio, the more 2M3MB produced during fermentation. Fermented solution obtained when valine, histidine, alanine, aspartic acid, aspartic acid, glutamine, glutamic acid, phenylalanine, cysteine, methionine, serine, leucine, or tyrosine was added to the test wheat juice (male usage ratio 25% by mass). The concentration of 2M3MB was 0.5 ppb or less, and it was found that the production of 2M3MB was suppressed by adding and fermenting these amino acids. On the other hand, when proline, lysine, tryptophan, or threonine was added to the test wort (malt usage ratio: 25% by mass), the 2M3MB concentration of the obtained fermented liquid was about the same as that without the addition of amino acids. It was suggested that the amino acids of threonine are not related to the production of 2M3MB. When glycine, arginine, or isoleucine is added to the test wort (malt usage ratio: 25% by mass), the 2M3MB concentration of the obtained fermentation broth is 1.4 ppb or more, and fermentation is performed by adding these amino acids. It was found that this promoted the production of 2M3MB.

試験用麦汁(麦芽使用比率100質量%)にグルタミンを添加した場合、得られた発酵液の2M3MB濃度は、試験用麦汁(麦芽使用比率25質量%)にグルタミンを添加した場合と同様に0.2ppbと非常に低かった。この結果から、特定のアミノ酸を添加することにより得られる2M3MBの生成抑制効果は、麦芽使用比率や発酵原料液の組成にはあまり影響されないことが示唆された。 When glutamine was added to the test wort (malt usage ratio 100% by mass), the 2M3MB concentration of the obtained fermented liquid was the same as when glutamine was added to the test wort (malt usage ratio 25% by mass). It was very low at 0.2 ppb. From this result, it was suggested that the effect of suppressing the production of 2M3MB obtained by adding a specific amino acid was not so affected by the malt usage ratio and the composition of the fermentation raw material solution.

[実施例2]
実施例1において、特に2M3MBの生成抑制効果が高かったアスパラギン酸、バリン、及びグルタミン酸について、麦汁に添加する量と2M3MBの生成抑制作用の強さの関係について調べた。
[Example 2]
In Example 1, aspartic acid, valine, and glutamic acid, which had a particularly high effect of suppressing the production of 2M3MB, were investigated for the relationship between the amount added to wort and the strength of the effect of suppressing the production of 2M3MB.

実施例1と同様にして調製した試験用麦汁(麦芽使用比率25質量%)に、アスパラギン酸、バリン、又はグルタミン酸をそれぞれ表4に記載の濃度となるように添加し、実施例1と同様にして発酵させ、得られた発酵液の2M3MB濃度を測定した。 Aspartic acid, valine, or glutamic acid was added to the test wort (malt usage ratio 25% by mass) prepared in the same manner as in Example 1 so as to have the concentrations shown in Table 4, respectively, and the same as in Example 1. And fermented, and the 2M3MB concentration of the obtained fermented liquid was measured.

Figure 0006930879
Figure 0006930879

各アミノ酸を添加した試験用麦汁(麦芽使用比率25質量%)から得られた発酵液の2M3MB濃度の測定結果を表1及び図1に示す。この結果、アスパラギン酸、バリン、及びグルタミン酸を添加したサンプルでは、いずれも添加量依存的に2M3MB濃度が低減していた。特にアミノ酸添加量が0.5mg/mL又は1.0mg/mLであるサンプルでは、得られた発酵液の2M3MB濃度が0.2ppb未満であり、タマネギ様臭は感じられなかった。 Table 1 and FIG. 1 show the measurement results of the 2M3MB concentration of the fermented liquid obtained from the test wort to which each amino acid was added (malt use ratio 25% by mass). As a result, in the samples to which aspartic acid, valine, and glutamic acid were added, the 2M3MB concentration was reduced depending on the amount of addition. In particular, in the sample in which the amount of amino acid added was 0.5 mg / mL or 1.0 mg / mL, the 2M3MB concentration of the obtained fermented liquid was less than 0.2 ppb, and no onion-like odor was felt.

Claims (6)

発酵工程を経て製造される発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの含有量を低減する方法であって、
酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、バリン、ヒスチジン、及びアラニンからなる群より選択される1種以上のアミノ酸を添加することを特徴とする、発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの低減方法。
A method for reducing the content of 2-mercapto-3-methyl-1-butanol in a fermented beer-like sparkling beverage produced through a fermentation process.
Fermented beer-like foaming characterized by adding one or more amino acids selected from the group consisting of valine, histidine, and alanine to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. A method for reducing 2-mercapto-3-methyl-1-butanol in a sex beverage.
発酵工程を経て製造される発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの含有量を低減する方法であって、
酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、アスパラギン、アスパラギン酸、グルタミン、グルタミン酸、バリン、ヒスチジン、及びアラニンからなる群より選択される1種以上のアミノ酸を添加することを特徴とする、発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの低減方法。
A method for reducing the content of 2-mercapto-3-methyl-1-butanol in a fermented beer-like sparkling beverage produced through a fermentation process.
To add one or more amino acids selected from the group consisting of aspartic acid, aspartic acid, glutamine, glutamic acid, valine, histidine, and alanine to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. 2. A method for reducing 2-mercapto-3-methyl-1-butanol in a fermented beer-like effervescent beverage.
発酵工程を経て製造される発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの含有量を低減する方法であって、
酵母を接種する前の発酵原料液又は前記発酵工程中の発酵液に、フェニルアラニン、システイン、メチオニン、セリン、ロイシン、及びチロシンからなる群より選択される1種以上のアミノ酸を添加することを特徴とする、発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの低減方法。
A method for reducing the content of 2-mercapto-3-methyl-1-butanol in a fermented beer-like sparkling beverage produced through a fermentation process.
It is characterized by adding one or more amino acids selected from the group consisting of phenylalanine, cysteine, methionine, serine, leucine, and tyrosine to the fermentation raw material solution before inoculating yeast or the fermentation solution during the fermentation step. A method for reducing 2-mercapto-3-methyl-1-butanol in a fermented beer-like effervescent beverage.
前記アミノ酸の総添加量が、前記発酵原料液又は前記発酵液1L当たり0.2g〜1.0gである、請求項1〜3のいずれか一項に記載の発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの低減方法。 2- Method for reducing mercapto-3-methyl-1-butanol. 前記アミノ酸の総添加量が、前記発酵原料液又は前記発酵液1L当たり1.0g以上である、請求項1〜3のいずれか一項に記載の発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの低減方法。 2-Mercapto-3 of the fermented beer-like effervescent beverage according to any one of claims 1 to 3, wherein the total amount of the amino acids added is 1.0 g or more per 1 L of the fermented raw material liquid or the fermented liquid. -Method for reducing methyl-1-butanol. 前記発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの含有量を、0.5ppb以下に低減する、請求項1〜3のいずれか一項に記載の発酵ビール様発泡性飲料の2−メルカプト−3−メチル−1−ブタノールの低減方法。 The fermented beer-like effervescent according to any one of claims 1 to 3, which reduces the content of 2-mercapto-3-methyl-1-butanol of the fermented beer-like effervescent beverage to 0.5 ppb or less. A method for reducing 2-mercapto-3-methyl-1-butanol in beverages.
JP2017168928A 2017-09-01 2017-09-01 Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages Active JP6930879B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2017168928A JP6930879B2 (en) 2017-09-01 2017-09-01 Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages
PCT/JP2018/025363 WO2019044163A1 (en) 2017-09-01 2018-07-04 Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2017168928A JP6930879B2 (en) 2017-09-01 2017-09-01 Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages

Publications (2)

Publication Number Publication Date
JP2019041688A JP2019041688A (en) 2019-03-22
JP6930879B2 true JP6930879B2 (en) 2021-09-01

Family

ID=65525397

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2017168928A Active JP6930879B2 (en) 2017-09-01 2017-09-01 Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages

Country Status (2)

Country Link
JP (1) JP6930879B2 (en)
WO (1) WO2019044163A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6930879B2 (en) * 2017-09-01 2021-09-01 アサヒビール株式会社 Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages
JP6674577B1 (en) * 2019-05-31 2020-04-01 サントリーホールディングス株式会社 Beer taste beverage

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW201237160A (en) * 2002-11-07 2012-09-16 Suntory Holdings Ltd Process for producing fermented drink
US20090186122A1 (en) * 2005-03-03 2009-07-23 Sapporo Breweries Limited Method of controlling the flavor of alcoholic drink
JP5399119B2 (en) * 2009-04-14 2014-01-29 アサヒビール株式会社 Yeast with reduced hydrogen sulfide production capacity
JP2011223951A (en) * 2010-04-22 2011-11-10 Asahi Breweries Ltd Brewing of beer yeast highly discharging sulfurous acid
JP6930879B2 (en) * 2017-09-01 2021-09-01 アサヒビール株式会社 Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages

Also Published As

Publication number Publication date
JP2019041688A (en) 2019-03-22
WO2019044163A1 (en) 2019-03-07

Similar Documents

Publication Publication Date Title
JP2017118824A (en) Fermented malt beverage and production method thereof
JP6329759B2 (en) Beer-taste beverage and method for producing the same
JP6282463B2 (en) Fermented malt beverage
JPWO2014156735A1 (en) Method for producing sparkling beverage
JP2021036921A (en) Method for improving sharpness in taste of beer-like sparkling beverage
JP2018183126A (en) Fermented malt beverage
JP6930879B2 (en) Method for reducing 2-mercapto-3-methyl-1-butanol in fermented beer-like effervescent beverages
JP7049821B2 (en) Method for manufacturing beer-like fermented malt beverage and method for improving foam retention of beer-like fermented malt beverage
JP6403380B2 (en) Method for producing a beer-taste fermented beverage
JP5855579B2 (en) Process for producing beer-like sparkling fermented beverages with high pyruvic acid content
JP7044703B2 (en) Method for manufacturing fermented beer-like sparkling beverage with suppressed off-flavour
JP6997532B2 (en) A method for producing a beer-like effervescent beverage and a method for improving the sharpness of a beer-like effervescent beverage.
JP6403381B2 (en) Method for reducing the aroma of malt fermented beverages
JP7201349B2 (en) Method for reducing off-flavor of fermented beer-like sparkling beverage
JP7245187B2 (en) Method for producing fermented malt beverage
JP6402382B2 (en) Non-fermented beer-taste beverage and method for producing the same
EP3604491B1 (en) Malt beverage having suppressed grain odor
JP6757439B2 (en) Beer taste fermented beverage and its manufacturing method
JP2018007604A (en) Beer taste beverage, method for producing beer taste beverage, and method for improving the flavor of beer taste beverage
JP6948835B2 (en) Malt beverage and its manufacturing method
WO2023171157A1 (en) Fermented beer-like effervescent beverage and method for manufacturing same
JP2020127374A (en) Beer-like sparkling drink, and production method thereof
JP2017147988A (en) Beer taste beverage, method for producing beer taste beverage, and method for improving flavor of beer taste beverage

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20200710

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20210720

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20210812

R150 Certificate of patent or registration of utility model

Ref document number: 6930879

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150