JP2018186716A - Fermented malt beverage - Google Patents
Fermented malt beverage Download PDFInfo
- Publication number
- JP2018186716A JP2018186716A JP2017089833A JP2017089833A JP2018186716A JP 2018186716 A JP2018186716 A JP 2018186716A JP 2017089833 A JP2017089833 A JP 2017089833A JP 2017089833 A JP2017089833 A JP 2017089833A JP 2018186716 A JP2018186716 A JP 2018186716A
- Authority
- JP
- Japan
- Prior art keywords
- fermented malt
- content
- raw material
- malt beverage
- fermented
- 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.)
- Granted
Links
- 235000021577 malt beverage Nutrition 0.000 title claims abstract description 91
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 claims abstract description 159
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- 239000002994 raw material Substances 0.000 claims abstract description 64
- 238000000855 fermentation Methods 0.000 claims abstract description 61
- 230000004151 fermentation Effects 0.000 claims abstract description 61
- GXCLVBGFBYZDAG-UHFFFAOYSA-N N-[2-(1H-indol-3-yl)ethyl]-N-methylprop-2-en-1-amine Chemical compound CN(CCC1=CNC2=C1C=CC=C2)CC=C GXCLVBGFBYZDAG-UHFFFAOYSA-N 0.000 claims abstract description 54
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Landscapes
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Abstract
Description
本発明は、発酵麦芽飲料において、麦芽使用比率がさほど高くない場合であっても飲み応えを改善する方法、及び当該方法により飲み応えが改善された発酵麦芽飲料に関する。 The present invention relates to a method for improving drinking response even when the malt use ratio is not so high in a fermented malt beverage, and a fermented malt beverage having improved drinking response by the method.
ビールや発泡酒等のビール様発泡性飲料は、消費者の嗜好の多様化にともない、多種多様の商品が上市されている。特に、近年の消費者の健康志向から、低カロリーや低糖質のビール様発泡性飲料に対する需要が高まっている。例えば、発酵工程を経て製造される発酵ビール様発泡性飲料の場合には、発酵原料として、酵母に対し非資化性の糖質を比較的多く含む麦芽の使用量を抑え、液糖のような非資化性の糖質を含まない糖類を多く使用することによって、飲料の糖質含有量やカロリーを低減させることができる。 A wide variety of beer-like sparkling beverages such as beer and sparkling liquor have been put on the market as consumer preferences diversify. In particular, the demand for low-calorie and low-sugar beer-like sparkling beverages has increased in recent years due to consumer health. For example, in the case of a fermented beer-like sparkling beverage produced through a fermentation process, the amount of malt containing a relatively large amount of non-assimilable saccharides for yeast is suppressed as a fermentation raw material. By using a large amount of saccharides that do not contain non-assimilable saccharides, the saccharide content and calories of the beverage can be reduced.
しかしながら、ビール等の麦芽を原料とする発酵ビール様発泡性飲料においては、飲み応えやコク感は、その多くを麦芽由来の香味成分に依存しているため、麦芽の使用比率が低い発酵麦芽飲料では、すっきりしたキレのある味感が強くなる一方で、味わいやコクが不足し易いという傾向がある。麦芽の使用比率が低い発酵麦芽飲料の製造方法としては、例えば、特許文献1に、発酵原料の一部として酵母エキスと玄米を用いる方法が開示されている。麦芽には、酵母による正常な発酵に必要なアミノ酸やミネラル類が多く含まれている。当該文献に記載の方法では、麦芽の使用比率を低くすることにより不足するアミノ酸等を酵母エキスにより補い、かつ玄米により酵母エキス由来の好ましくない臭いや味を低減させている。 However, in fermented beer-like effervescent beverages made from malt such as beer, the drinking response and richness depend on malt-derived flavor components, and therefore fermented malt beverages with a low malt use ratio However, there is a tendency that the taste and richness are likely to be insufficient while the refreshing taste is strong. As a method for producing a fermented malt beverage having a low malt use ratio, for example, Patent Document 1 discloses a method of using a yeast extract and brown rice as part of a fermentation raw material. Malt is rich in amino acids and minerals necessary for normal fermentation by yeast. In the method described in the said literature, the amino acid etc. which are insufficient by lowering the use ratio of malt are supplemented with a yeast extract, and the unpleasant smell and taste derived from a yeast extract are reduced with brown rice.
本発明は、麦芽使用比率がさほど高くない発酵麦芽飲料であっても飲み応えを改善する方法、及び当該方法により製造された発酵麦芽飲料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 improving drinking response even if it is a fermented malt beverage having a low malt use ratio, and a fermented malt beverage produced by the method.
本発明者らは、上記課題を解決すべく鋭意研究した結果、発酵麦芽飲料において、飲料中のジメチルスルフィド(DMS)と3−メチル−2−ブテン−1−チオール(MBT)の含有量を所定の範囲内に調整することによって、麦芽の使用比率を高めることなく、飲み応えを改善できることを見出し、本発明を完成させた。 As a result of intensive studies to solve the above problems, the present inventors have determined the contents of dimethyl sulfide (DMS) and 3-methyl-2-butene-1-thiol (MBT) in the beverage in the fermented malt beverage. By adjusting within the range, it was found that the drinking response could be improved without increasing the use ratio of malt, and the present invention was completed.
本発明に係る発酵麦芽飲料、発酵麦芽飲料の製造方法、及び発酵麦芽飲料の飲み応えを改善する方法は、下記[1]〜[7]である。
[1] DMS含有量が15ppb以上であり、MBT含有量が5ppt以上であることを特徴とする、発酵麦芽飲料。
[2] DMS含有量が120ppb以下である、前記[1]の発酵麦芽飲料。
[3] MBT含有量が120ppt以下である、前記[1]又は[2]の発酵麦芽飲料。
[4] 遮光容器詰飲料である、前記[1]〜[3]のいずれかの発酵麦芽飲料。
[5] 麦芽を含む発酵原料と水とを含む混合物を糖化処理し、得られた糖化液を煮沸処理して発酵原料液を調製する仕込工程と、
得られた発酵原料液に酵母を接種して発酵させる発酵工程と、
を有し、
DMS含有量が15ppb以上であり、MBT含有量が5ppt以上である発酵麦芽飲料を製造することを特徴とする、発酵麦芽飲料の製造方法。
[6] 前記発酵原料に占める麦芽の使用比率が100質量%未満である、前記[5]の発酵麦芽飲料の製造方法。
[7] 発酵麦芽飲料の飲み応えを改善するために、飲料中のDMS及びMBTの含有量を、
DMS含有量が15ppb以上及びMBT含有量が5ppt以上となるように調整することを特徴とする、発酵麦芽飲料の飲み応えを改善する方法。
The method for improving the drinking response of the fermented malt beverage, the fermented malt beverage, and the fermented malt beverage according to the present invention are the following [1] to [7].
[1] A fermented malt beverage characterized by having a DMS content of 15 ppb or more and an MBT content of 5 ppt or more.
[2] The fermented malt beverage according to [1], wherein the DMS content is 120 ppb or less.
[3] The fermented malt beverage according to [1] or [2], wherein the MBT content is 120 ppt or less.
[4] The fermented malt beverage according to any one of [1] to [3], which is a light-shielded container-packed beverage.
[5] A saccharification treatment of a mixture containing a fermentation raw material containing malt and water, a preparation step of preparing a fermentation raw material solution by boiling the obtained saccharified solution,
A fermentation process in which yeast is inoculated and fermented to the obtained fermentation raw material liquid;
Have
A method for producing a fermented malt beverage, comprising producing a fermented malt beverage having a DMS content of 15 ppb or more and an MBT content of 5 ppt or more.
[6] The method for producing a fermented malt beverage according to [5], wherein a use ratio of malt in the fermentation raw material is less than 100% by mass.
[7] In order to improve the drinking response of the fermented malt beverage, the contents of DMS and MBT in the beverage are
A method for improving the drinking response of a fermented malt beverage, comprising adjusting the DMS content to be 15 ppb or more and the MBT content to be 5 ppt or more.
本発明により、麦芽の使用比率を高めることなく、飲み応えが改善された発酵麦芽飲料を提供できる。 According to the present invention, it is possible to provide a fermented malt beverage with improved drinking response without increasing the use ratio of malt.
本発明及び本願明細書における発酵麦芽飲料とは、麦芽を発酵原料とし、発酵工程を経て製造される飲料を意味する。本発明における発酵麦芽飲料のアルコール濃度は限定されず、1.0容量%以上のアルコール飲料であってもよく、1.0容量%未満のいわゆるノンアルコール飲料であってもよい。 The fermented malt beverage in the present invention and the specification of the present application means a beverage produced by using malt as a fermentation raw material and undergoing a fermentation process. The alcohol concentration of the fermented malt beverage in the present invention is not limited, and may be an alcoholic beverage of 1.0% by volume or more, or a so-called non-alcoholic beverage of less than 1.0% by volume.
本発明における発酵麦芽飲料としては、特にビール様発泡性飲料であることが好ましい。ビール様発泡性飲料とは、ビールらしさ(香味上ビールを想起させる呈味)を有する発泡性飲料を意味する。ビール様発泡性飲料である発酵麦芽飲料としては、具体的には、ビール、麦芽を原料として発酵工程を経て製造された発泡酒、麦芽を原料として発酵工程を経て製造されたノンアルコールビール等が挙げられる。本発明における発酵麦芽飲料としては、麦芽を原料として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。 The fermented malt beverage in the present invention is particularly preferably a beer-like sparkling beverage. A beer-like effervescent beverage means an effervescent beverage having a beer-like character (taste reminiscent of beer on flavor). As fermented malt beverages that are beer-like sparkling beverages, specifically, beer, sparkling liquor produced through the fermentation process using malt as a raw material, non-alcohol beer produced through the fermentation process using malt as a raw material, etc. Can be mentioned. The fermented malt beverage in the present invention may be a liqueur obtained by mixing a beverage produced through a fermentation process using malt as a raw material with an alcohol-containing distillate.
なお、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、一般に蒸留酒に分類されるものを用いることができる。例えば、原料用アルコール、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、焼酎等を用いることができる。 The alcohol-containing distillate is a solution containing an alcohol obtained by a distillation operation, and those generally classified as distilled liquor can be used. For example, raw material alcohol, spirits, whiskey, brandy, vodka, rum, tequila, gin, shochu, etc. can be used.
本発明に係る発酵麦芽飲料は、DMS含有量が15ppb以上であり、MBT含有量が5ppt以上であることを特徴とする。発酵麦芽飲料中のDMSとMBTの含有量をそれぞれ前記範囲内に調整することによって、麦芽の使用比率を高めることなく、飲み応え(コク)を改善できる。DMSは、麦芽由来のビールのオフフレーバーであり、麦汁の煮沸温度が低い場合に生成されやすい。MBTは、「日光臭」といわれるホップ等に由来するビールのオフフレーバーである。このように、ビールのオフフレーバーとして知られている香気成分の含有量を調整することによって、エキス分を増加させることなく、飲み応えが改善できることは、本発明者によって初めて見出された知見である。 The fermented malt beverage according to the present invention has a DMS content of 15 ppb or more and an MBT content of 5 ppt or more. By adjusting the contents of DMS and MBT in the fermented malt beverage within the above ranges, the drinking response (brightness) can be improved without increasing the use ratio of the malt. DMS is an off-flavor of malt-derived beer and is easily generated when the boiling temperature of wort is low. MBT is an off-flavor of beer derived from hops or the like called “sunlight smell”. Thus, by adjusting the content of the aroma component known as beer off-flavor, it is possible to improve the drinking response without increasing the extract, based on the knowledge first discovered by the present inventors. is there.
本発明に係る発酵麦芽飲料のDMS含有量は、15ppb以上の範囲内であれば特に限定されるものではない。充分な飲み応え改善効果とビールらしい香味に優れていることから、本発明に係る発酵麦芽飲料のDMS含有量としては、15ppb以上120ppb以下が好ましく、15ppb以上100ppb以下がより好ましく、15ppb以上40ppb以下がさらに好ましい。 The DMS content of the fermented malt beverage according to the present invention is not particularly limited as long as it is within the range of 15 ppb or more. The DMS content of the fermented malt beverage according to the present invention is preferably 15 ppb or more and 120 ppb or less, more preferably 15 ppb or more and 100 ppb or less, and more preferably 15 ppb or more and 40 ppb or less because it has a sufficient drinking response improvement effect and a beer-like flavor. Is more preferable.
本発明に係る発酵麦芽飲料のDMS含有量は、例えば、DMSを添加剤として添加することにより調整することができる。添加剤として添加するDMSは、合成されたDMSでもよく、天然物から抽出・精製されたDMSでもよい。また、DMSをその他の成分と共に含有する香料であってもよい。 The DMS content of the fermented malt beverage according to the present invention can be adjusted, for example, by adding DMS as an additive. The DMS added as an additive may be a synthesized DMS or a DMS extracted and purified from a natural product. Moreover, the fragrance | flavor which contains DMS with another component may be sufficient.
本発明に係る発酵麦芽飲料のDMS含有量は、DMSを原料として直接添加せずとも、製造条件を適宜調整することによっても調整することができる。DMSは、麦汁の煮沸処理によって主に麦芽由来のS−メチオニルメチオニンが分解され生成される。このため、例えば、DMS含有量は、原料とする麦芽として、元々DMSの含有量が同種の他の品種等よりも高いものを選択して用いたり、麦芽の使用量を調整することにより、調整することができる。また、DMSは、酵母による含硫化合物の代謝によっても産生されるため、発酵条件を適宜調整することによっても、発酵麦芽飲料のDMS含有量を調整することができる。 The DMS content of the fermented malt beverage according to the present invention can be adjusted by appropriately adjusting the production conditions without directly adding DMS as a raw material. DMS is produced mainly by decomposition of malt-derived S-methionylmethionine by boiling treatment of wort. For this reason, for example, the DMS content is adjusted by selecting and using a malt as a raw material that is originally higher in content of DMS than other varieties of the same type, or adjusting the amount of malt used. can do. Moreover, since DMS is produced also by metabolism of the sulfur-containing compound by yeast, the DMS content of the fermented malt beverage can also be adjusted by appropriately adjusting the fermentation conditions.
本発明に係る発酵麦芽飲料のDMSの含有量は、例えば、炎光光度検出器を用いたガスクロマトグラフィー(Gas Chromatography−Flame Photometric Detector;GC−FPD)分析により測定することができる。具体的には、まず、サンプルをスターラーバーの入ったバイアル瓶に入れ、所定量の塩化ナトリウムを加え、次いで3N塩酸、内部標準液(硫化エチルメチル10mg/mL)を所定量ずつ加えた後、アルミキャップで密栓する。密栓した状態で、室温で10分間スターラーバーを回転させて撹拌することにより塩化ナトリウムを溶解させたサンプルを、ヘッドスペースGC−FPDに供し、内部標準比からサンプルのDMS濃度を定量する。 The content of DMS in the fermented malt beverage according to the present invention can be measured by, for example, gas chromatography (Gas Chromatography-Flame Photometric Detector; GC-FPD) analysis using a flame photometric detector. Specifically, first, a sample is put into a vial containing a stirrer bar, a predetermined amount of sodium chloride is added, and then 3N hydrochloric acid and an internal standard solution (ethyl methyl sulfide 10 mg / mL) are added in a predetermined amount. Seal with an aluminum cap. A sample in which sodium chloride is dissolved by rotating the stirrer bar for 10 minutes at room temperature while stirring in a sealed state is applied to the headspace GC-FPD, and the DMS concentration of the sample is quantified from the internal standard ratio.
本発明に係る発酵麦芽飲料のMBT含有量は、5ppt以上の範囲内であれば特に限定されるものではない。充分な飲み応え改善効果とビールらしい香味に優れていることから、本発明に係る発酵麦芽飲料のDMS含有量としては、5ppt以上120ppt以下が好ましく、5ppt以上100ppt以下がより好ましく、5ppt以上15ppt以下がさらに好ましい。 The MBT content of the fermented malt beverage according to the present invention is not particularly limited as long as it is within the range of 5 ppt or more. The DMS content of the fermented malt beverage according to the present invention is preferably 5 ppt or more and 120 ppt or less, more preferably 5 ppt or more and 100 ppt or less, and more preferably 5 ppt or more and 15 ppt or less because it has a sufficient drinking response improvement effect and a beer-like flavor. Is more preferable.
本発明に係る発酵麦芽飲料のMBT含有量は、例えば、MBTを添加剤として添加することにより調整することができる。添加剤として添加するMBTは、合成されたMBTでもよく、天然物から抽出・精製されたMBTでもよい。また、MBTをその他の成分と共に含有する香料であってもよい。 The MBT content of the fermented malt beverage according to the present invention can be adjusted, for example, by adding MBT as an additive. The MBT added as an additive may be a synthesized MBT or an MBT extracted and purified from a natural product. Moreover, the fragrance | flavor which contains MBT with another component may be sufficient.
本発明に係る発酵麦芽飲料のMBT含有量は、MBTを原料として直接添加せずとも、製造条件を適宜調整することによっても調整することができる。MBTは、紫外線〜可視光線によりイソα酸のアリル側鎖が光分解を受けた結果に生じたラジカルと含硫化合物から生じたラジカルとから生成される。ホップを原料とする場合、イソα酸は、ホップを麦汁に添加して煮沸処理することにより、イソα酸を含む発酵原料液が調製される。このため、原料として用いるホップの種類や使用量、煮沸条件を適宜調整することによって、発酵原料液中のイソα酸の含有量を調整することができ、ひいては最終的に飲料中に含まれるMBT含有量を調整することができる。また、MBTは、酵母による含硫化合物の代謝によっても産生されるため、発酵条件を適宜調整することによっても、発酵麦芽飲料のMBT含有量を調整することができる。さらに、発酵麦芽飲料に照射する日光量を調整することによっても、当該発酵麦芽飲料のMBT含有量を調整することができる。 The MBT content of the fermented malt beverage according to the present invention can be adjusted by appropriately adjusting the production conditions without directly adding MBT as a raw material. MBT is generated from radicals generated as a result of photolysis of the allyl side chain of isoalpha acid by ultraviolet to visible light and radicals generated from sulfur-containing compounds. When hop is used as a raw material, isoalpha acid is prepared by adding hop to wort and boiling to prepare a fermentation raw material liquid containing isoalpha acid. For this reason, content of iso alpha acid in a fermentation raw material liquid can be adjusted by adjusting suitably the kind of hop used as a raw material, usage-amount, and boiling conditions, and eventually MBT contained in a drink finally. The content can be adjusted. Moreover, since MBT is produced also by metabolism of the sulfur-containing compound by yeast, the MBT content of the fermented malt beverage can also be adjusted by appropriately adjusting the fermentation conditions. Furthermore, the MBT content of the fermented malt beverage can also be adjusted by adjusting the amount of sunlight irradiated to the fermented malt beverage.
本発明に係る発酵麦芽飲料のMBTの含有量は、例えば、供試サンプルから含硫化合物を水銀等の重金属化合物に結合させた後、強陰イオン交換樹脂カラムに吸着させる。その後、システインにより当該カラムから溶出させた含硫化合物を、質量分析計を搭載したGC(GC/MS)分析し、内部標準比から当該供試サンプルのMBT濃度を定量する。 The content of MBT of the fermented malt beverage according to the present invention is, for example, after adsorbing a sulfur-containing compound from a test sample to a heavy metal compound such as mercury and then adsorbing it on a strong anion exchange resin column. Thereafter, the sulfur-containing compound eluted from the column with cysteine is subjected to GC (GC / MS) analysis equipped with a mass spectrometer, and the MBT concentration of the test sample is quantified from the internal standard ratio.
本発明に係る発酵麦芽飲料は、飲料中のDMS含有量とMBT含有量を所定の範囲内に調整する以外は、一般的な発酵麦芽飲料と同様にして製造できる。一般的な発酵麦芽飲料は、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。 The fermented malt beverage according to the present invention can be produced in the same manner as a general fermented malt beverage, except that the DMS content and MBT content in the beverage are adjusted within a predetermined range. A general fermented malt beverage can be produced by a process of preparation (preparation of fermentation raw material liquid), fermentation, storage, and filtration.
発酵原料としては、少なくとも麦芽を用いていればよく、麦芽のみを用いてもよく、麦芽以外の発酵原料を用いてもよい。発酵原料として用いる麦芽は、大麦麦芽であってもよく、小麦麦芽であってもよく、両者を併用してもよい。本発明の効果がより効果的に発揮できることから、本発明の発酵麦芽飲料は、発酵原料として、麦芽と麦芽以外の原料を併用するもの、すなわち、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%未満であることが好ましい。中でも、よりコクが強く、ビールらしい風味に優れるため、麦芽使用比率が20〜90質量%であることが好ましく、26〜90質量%であることがより好ましく、26〜66質量%であることがさらに好ましい。 As a fermentation raw material, at least malt may be used, only malt may be used, and fermentation raw materials other than malt may be used. The malt used as a fermentation raw material may be barley malt, wheat malt, or a combination of both. Since the effect of the present invention can be exhibited more effectively, the fermented malt beverage of the present invention uses, as a fermentation raw material, a combination of malt and raw materials other than malt, that is, malt use ratio (use of malt in the entire fermentation raw material) The ratio of the amount is preferably less than 100% by mass. Among them, because it is stronger and has a beer-like flavor, the malt use ratio is preferably 20 to 90% by mass, more preferably 26 to 90% by mass, and 26 to 66% by mass. Further preferred.
麦芽以外の発酵原料としては、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。糖質原料としては、例えば、液糖等の糖類が挙げられる。また、穀物原料としては、例えば、大麦や小麦等の麦芽以外の麦類、米、トウモロコシ、大豆等の豆類、イモ類等が挙げられ、大麦が特に好ましい。また、本発明において用いられる麦芽以外の穀物原料としては、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。 As a fermentation raw material other than malt, only a cereal raw material may be used, only a saccharide raw material may be used, or both may be used in combination. Examples of the saccharide raw material include saccharides such as liquid sugar. Examples of the grain raw material include barley other than malt such as barley and wheat, beans such as rice, corn, and soybean, and potatoes, and barley is particularly preferable. Moreover, as a grain raw material other than malt used in the present invention, one kind of grain raw material may be used, or a mixture of a plurality of kinds of grain raw materials may be used.
麦芽をはじめとする各穀物原料は、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、麦芽破砕物、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。 Each grain raw material including malt can be used as a grain syrup, a grain extract or the like, but is preferably used as a ground grain product obtained by grinding. Grain pulverization can be carried out by a conventional method. The pulverized cereal may be a crushed product such as malt crushed material, corn starch, corn grits or the like, which has been subjected to a treatment usually performed before and after the pulverization treatment.
仕込工程(発酵原料液調製工程)として、発酵原料から発酵原料液を調製する。具体的には、まず、発酵原料と原料水とを含む混合物を調製して加温し、発酵原料の澱粉質を糖化させる。当該混合物には、発酵原料等と水以外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、酵母エキス、タンパク質分解物、水溶性食物繊維、甘味料、苦味料、果汁、着色料、香草、香料等が挙げられる。 As a preparation process (fermentation raw material liquid preparation process), a fermentation raw material liquid is prepared from a fermentation raw material. Specifically, first, a mixture containing a fermentation raw material and raw water is prepared and heated to saccharify the starch material of the fermentation raw material. You may add auxiliary raw materials other than fermentation raw material etc. and water to the said mixture. Examples of the auxiliary material include hop, yeast extract, protein degradation product, water-soluble dietary fiber, sweetener, bitter, fruit juice, coloring, herb, and fragrance.
水溶性食物繊維とは、水に溶解し、かつヒトの消化酵素により消化されない又は消化され難い炭水化物を意味する。本発明において用いられる水溶性食物繊維としては、例えば、難消化性デキストリン、ポリデキストロース、大豆食物繊維、ガラクトマンナン、イヌリン、グアーガム分解物、ペクチン、アラビアゴム等が挙げられる。これらの水溶性食物繊維は、1種類のみを用いてもよく、2種類以上を併用してもよい。 By water-soluble dietary fiber is meant a carbohydrate that is soluble in water and is not or is difficult to digest by human digestive enzymes. Examples of the water-soluble dietary fiber used in the present invention include indigestible dextrin, polydextrose, soybean dietary fiber, galactomannan, inulin, guar gum degradation product, pectin, gum arabic and the like. These water-soluble dietary fibers may use only 1 type and may use 2 or more types together.
甘味料としては、砂糖であってもよく、比較的甘味度の低いものであってもよく、高甘味度甘味料であってもよい。比較的甘味度の低い甘味料としては、具体的には、多糖類、甘味系アミノ酸が挙げられる。多糖類とは、3以上の単糖が重合した糖質を意味する。多糖類は、主にその大きさによって、でんぷん、デキストリン、及びオリゴ糖に大別される。オリゴ糖は、3〜10個程度の単糖が重合した糖質であり、デキストリンは、でんぷんを加水分解して得られる糖質であって、オリゴ糖よりも大きなものを指す。甘味系アミノ酸としては、アラニンやグリシンが挙げられ、アラニンが好ましい。高甘味度甘味料としては、アセスルファムカリウム、ネオテーム、アスパルテーム、スクラロース、ステビア、酵素処理ステビア等が挙げられる。これらの甘味料は、1種類のみを用いてもよく、2種類以上を併用してもよい。 The sweetener may be sugar, may have a relatively low sweetness, or may be a high sweetness sweetener. Specific examples of sweeteners having a relatively low sweetness include polysaccharides and sweet amino acids. The polysaccharide means a saccharide obtained by polymerizing three or more monosaccharides. Polysaccharides are roughly classified into starch, dextrin, and oligosaccharide mainly depending on the size. An oligosaccharide is a saccharide in which about 3 to 10 monosaccharides are polymerized, and a dextrin is a saccharide obtained by hydrolyzing starch, which is larger than the oligosaccharide. Examples of the sweet amino acid include alanine and glycine, and alanine is preferable. Examples of high-intensity sweeteners include acesulfame potassium, neotame, aspartame, sucralose, stevia, and enzyme-treated stevia. These sweeteners may use only 1 type and may use 2 or more types together.
苦味料としては、製品である発酵麦芽飲料において、ビールと同質若しくは近似する苦味を呈するものであれば特に限定されるものではなく、ホップ中に含まれている苦味成分であってもよく、ホップには含まれていない苦味成分であってもよい。当該苦味料としては、具体的には、マグネシウム塩、カルシウム塩、クエン酸トリブチル、クエン酸トリエチル、ナリンジン、クワシン、イソα酸、テトライソα酸、β酸の酸化物、キニーネ、モモルデシン、クエルシトリン、テオブロミン、カフェイン等の苦味付与成分、及びゴーヤ、センブリ茶、苦丁茶、ニガヨモギ抽出物、ゲンチアナ抽出物、キナ抽出物等の苦味付与素材が代表的に挙げられる。これらの苦味料は、1種類のみを用いてもよく、2種類以上を併用してもよい。 The bittering agent is not particularly limited as long as it exhibits the same or similar bitterness as beer in the fermented malt beverage as a product, and may be a bitterness component contained in hops. It may be a bitter component that is not contained in. As the bittering agent, specifically, magnesium salt, calcium salt, tributyl citrate, triethyl citrate, naringin, quassin, iso-α acid, tetraiso-α acid, β-acid oxide, quinine, momordesine, quercitrin, Representative examples include bitterness-imparting ingredients such as theobromine and caffeine, and bitterness-imparting materials such as bitter gourd, senburi tea, bitter tea, nigamomogi extract, gentian extract, and kina extract. These bitterings may use only 1 type and may use 2 or more types together.
タンパク質分解物としては、例えば、大豆タンパク分解物等が挙げられる。
着色料としては、例えば、カラメル色素等が挙げられる。
香料としては、例えば、ビールフレーバー、ビール香料、ホップ香料等が挙げられる。
Examples of protein degradation products include soy protein degradation products.
Examples of the colorant include caramel color.
Examples of the flavor include beer flavor, beer flavor, and hop flavor.
仕込工程においては、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好ましい。これらの酵素により、発酵原料中の非資化性糖を、資化性糖への分解反応が促進され、麦芽使用比率が高い発酵原料を用いた場合でも、非資化性糖の含有量が低く抑えられた発酵原料液を調製することができる。 In the preparation step, it is preferable to add a saccharifying enzyme such as α-amylase, glucoamylase, or pullulanase, or an enzyme agent such as protease. These enzymes promote the decomposition reaction of non-assimilable sugars in fermentation raw materials into assimilating sugars, and even when fermenting raw materials with a high malt use ratio are used, the content of non-assimilable sugars is reduced. A fermentation raw material liquid suppressed to a low level can be prepared.
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、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。糖化処理の時間を調節することにより、糖化効率を制御し、最終的に得られる発酵麦芽飲料の糖質含有量を所望の範囲内に調整することもできる。 The saccharification treatment is performed using an enzyme derived from a grain raw material or the like, or an enzyme added separately. The temperature and time during the saccharification treatment take into account the type of cereal raw material used, the proportion of cereal raw material in the total fermentation raw material, the type of enzyme added and the amount of the mixture, the quality of the desired fermented malt beverage, etc. , Adjusted as appropriate. For example, the saccharification treatment can be performed by a conventional method such as holding a mixture containing grain raw materials and the like at 35 to 70 ° C. for 20 to 90 minutes. By adjusting the saccharification time, the saccharification efficiency can be controlled, and the sugar content of the finally obtained fermented malt beverage can be adjusted within a desired range.
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 boiled juice (boiled sugar solution) can be prepared. The sugar solution is preferably filtered before boiling, and the obtained filtrate is preferably boiled. Moreover, you may boil this using the thing which added warm water to the malt extract instead of the filtrate of this sugar liquid. The boiling method and its conditions can be determined as appropriate.
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)及び煮沸条件は、適宜決定することができる。 A fermented malt beverage having a desired flavor can be produced by appropriately adding herbs before or during the boiling treatment. In particular, hops are preferably added before or during the boiling process. By boiling in the presence of hops, the hop flavor and aroma components can be efficiently boiled. The addition amount of hops, the addition mode (for example, adding in several steps) and the boiling conditions can be determined as appropriate.
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50〜100℃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 process and before the fermentation process, it is preferable to remove protein and other soot produced by precipitation from the prepared broth. The removal of the soot may be performed by any solid-liquid separation process, but in general, the precipitate is removed using a tank called a whirlpool. The temperature of the broth in this case should just be 15 degreeC or more, and is generally performed at about 50-100 degreeC. The broth (filtrate) after removing the koji is cooled to an appropriate fermentation temperature with a plate cooler or the like. The broth after removing this koji 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。 Next, as a fermentation process, 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 process as it is, or may be subjected to the fermentation process after adjusting to a desired extract concentration. The yeast used for fermentation is not particularly limited, and can be appropriately selected from yeasts used for producing alcoholic beverages. Although it may be a top fermentation yeast or a bottom fermentation yeast, it is preferably a bottom fermentation yeast because it can be easily applied to large-scale brewing facilities.
さらに、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た後、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0.4〜1.0μm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。また、所望のアルコール濃度とするために、濾過前又は濾過後に適量の加水を行って希釈してもよい。得られた発酵麦芽飲料は、通常、充填工程により容器詰めされて、製品として出荷される。本発明に係る発酵麦芽飲料は、保存中のMBTの予期せぬ増量を抑制するため、缶等の遮光容器に充填することが好ましい。 Furthermore, as a sake storage process, the obtained fermented liquor is aged in a storage tank, stored and stabilized under a low temperature condition of about 0 ° C., and then filtered as a filtration process. The target fermented malt beverage can be obtained by removing yeast and proteins insoluble in the temperature range. The said filtration process should just be a method which can filter and remove yeast, for example, diatomaceous earth filtration, filter filtration with a filter whose average pore diameter is about 0.4-1.0 micrometer etc. are mentioned. Further, in order to obtain a desired alcohol concentration, an appropriate amount of water may be added and diluted before or after filtration. The obtained fermented malt beverage is usually packed in a container by a filling process and shipped as a product. The fermented malt beverage according to the present invention is preferably filled in a light-shielding container such as a can in order to suppress an unexpected increase in MBT during storage.
その他、酵母による発酵工程以降の工程において、例えばアルコール含有蒸留液と混和することにより、酒税法におけるリキュール類に相当する発酵麦芽飲料を製造することができる。アルコール含有蒸留液の添加は、アルコール濃度の調整のための加水前であってもよく、加水後であってもよい。添加するアルコール含有蒸留液は、より好ましい麦感を有する発酵麦芽飲料を製造し得ることから、麦スピリッツが好ましい。 In addition, in the process after the fermentation process by yeast, for example, by mixing with an alcohol-containing distillate, a fermented malt beverage corresponding to liqueurs in the liquor tax law can be produced. The addition of the alcohol-containing distillate may be before or after addition for adjusting the alcohol concentration. Since the alcohol-containing distillate to be added can produce a fermented malt beverage having a more preferable malt feeling, wheat spirits are preferred.
DMS又はこれを含有する香料やMBT又はこれを含有する香料を原料とする場合には、添加したDMS及びMBTが製造工程中で失われることを抑制するために、DMS及びMBTは、発酵原料液の煮沸処理後の任意の時点において添加することが好ましく、貯酒工程又はその後の濾過工程において添加することがより好ましい。 When using DMS or a fragrance containing MBS or a fragrance containing this as a raw material, in order to prevent the added DMS and MBT from being lost during the manufacturing process, DMS and MBT are used as a fermentation raw material liquid. It is preferable to add at an arbitrary time after the boiling treatment, and it is more preferable to add it at the alcohol storage step or the subsequent filtration step.
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。 EXAMPLES Next, although an Example and a reference example are shown and this invention is demonstrated further in detail, this invention is not limited to a following example etc.
<DMS濃度の測定>
以降の実施例において、DMSの濃度は、GC−FPD分析により測定した。
具体的には、まず、供試サンプルをスターラーバーの入ったバイアル瓶に入れ、所定量の塩化ナトリウムを加え、次いで3N塩酸、内部標準液(硫化エチルメチル10mg/mL)を所定量ずつ加えた後、アルミキャップで密栓した。密栓した状態で、室温で10分間スターラーバーを回転させて撹拌することにより塩化ナトリウムを溶解させた供試サンプルを、ヘッドスペースGC−FPDに供し、内部標準比から供試サンプルのジメチルスルフィド濃度を定量した。
<Measurement of DMS concentration>
In the following examples, the concentration of DMS was measured by GC-FPD analysis.
Specifically, first, the test sample was put in a vial bottle containing a stirrer bar, a predetermined amount of sodium chloride was added, and then 3N hydrochloric acid and an internal standard solution (ethyl methyl sulfide 10 mg / mL) were added in a predetermined amount. After that, it was sealed with an aluminum cap. A sample sample in which sodium chloride was dissolved by stirring and rotating the stir bar for 10 minutes at room temperature in a sealed state was applied to the headspace GC-FPD, and the dimethyl sulfide concentration of the sample sample was determined from the internal standard ratio. Quantified.
<MBT濃度の測定>
以降の実施例において、MBTの濃度は、GC/MS分析により測定した。
供試サンプル500mLに、0.1M Trisに溶解させた2mM p−HMB(p−ヒドロキシ水銀安息香酸)25mLと20mM tert−ブチル−4−メトキシフェノール(BHA)エタノール溶液 500μLと、内部標準液である500ng/mL 4−メトキシ−2−メチル−2−メルカプトブタン(4M4M2MB)エタノール溶液100mLとを添加し、密栓して、スターラーバーで室温10分間、強く攪拌し、供試サンプル中の含硫化合物を、水銀化合物であるp−HMBに吸着させた。この反応物をDowex−1(強陰イオン交換樹脂)カラムに吸着させた後、0.2mM tert−ブチル−4−メトキシフェノールを含有する0.1M酢酸ナトリウム緩衝液(pH6)100mLで当該カラムを洗浄した後、10mg/mL L−システイン塩酸塩一水和物を含有する0.1M 酢酸ナトリム緩衝液(pH6)100mLにより、含硫化合物をカラムから溶出させた。回収された溶出液を、酢酸エチル0.5mL、次いでジクロロメタン5mLで2回抽出し、回収された有機溶媒層を無水硫酸ナトリウムで脱水した後、窒素ガスにて100μLまで濃縮し、質量分析計を搭載したGC分析に供してMBTを定量した。
<Measurement of MBT concentration>
In the following examples, the concentration of MBT was measured by GC / MS analysis.
An internal standard solution of 500 mL of a test sample, 25 mL of 2 mM p-HMB (p-hydroxymercurybenzoic acid) dissolved in 0.1 M Tris, 500 μL of 20 mM tert-butyl-4-methoxyphenol (BHA) ethanol solution Add 500 ng / mL 4-methoxy-2-methyl-2-mercaptobutane (4M4M2MB) ethanol solution (100 mL), seal tightly and stir vigorously with a stir bar at room temperature for 10 minutes to remove the sulfur-containing compound in the test sample. And adsorbed on p-HMB which is a mercury compound. After adsorbing this reaction product to a Dowex-1 (strong anion exchange resin) column, the column was added with 100 mL of 0.1 M sodium acetate buffer (pH 6) containing 0.2 mM tert-butyl-4-methoxyphenol. After washing, the sulfur-containing compound was eluted from the column with 100 mL of 0.1 M sodium acetate buffer (pH 6) containing 10 mg / mL L-cysteine hydrochloride monohydrate. The recovered eluate was extracted twice with 0.5 mL of ethyl acetate and then with 5 mL of dichloromethane, and the recovered organic solvent layer was dehydrated with anhydrous sodium sulfate and then concentrated to 100 μL with nitrogen gas. MBT was quantified by GC analysis.
[実施例1]
発酵麦芽飲料に、DMS及びMBTを添加し、飲み応えに対する影響を調べた。
[Example 1]
DMS and MBT were added to the fermented malt beverage, and the effect on drinking response was examined.
まず、10kgの麦芽に原料水を混合した混合物を常法に従って加温して糖化液を製造した。得られた糖化液を濾過し、得られた濾液に25kgの液糖(固形分75質量%)、1kgの大豆タンパク質、及びホップを添加した後、煮沸して麦汁(穀物煮汁)を得た(麦芽使用比率:27質量%)。得られた麦汁を沈降槽に移して沈殿物を分離、除去した後、原麦汁エキスが12質量%となるように加水調整したものを発酵原料液とした。得られた発酵原料液200Lを約7℃に冷却した後、当該冷麦汁にビール酵母を接種し、約10℃で7日間発酵させた後、7日間貯酒タンク中で熟成させた。熟成後の発酵液をフィルター濾過(平均孔径:0.65μm)し、発酵麦芽飲料Aを得た。この発酵麦芽飲料Aは、アルコール度数5容量%、炭酸ガス圧0.23MPa、DMS含有量10ppb、MBT含有量3pptであった。 First, a mixture of raw material water mixed with 10 kg of malt was heated according to a conventional method to produce a saccharified solution. The obtained saccharified solution was filtered, and 25 kg of liquid sugar (solid content: 75% by mass), 1 kg of soy protein, and hop were added to the obtained filtrate, followed by boiling to obtain wort (cereal broth). (Mort use ratio: 27 mass%). The obtained wort was transferred to a settling tank, and the precipitate was separated and removed, and then the water was adjusted so that the original wort extract would be 12% by mass as the fermentation raw material liquid. After cooling the obtained fermentation raw material liquid 200L to about 7 ° C., the cold wort was inoculated with beer yeast, fermented at about 10 ° C. for 7 days, and then aged in a storage tank for 7 days. The fermented liquid after aging was filtered (average pore size: 0.65 μm) to obtain fermented malt beverage A. This fermented malt beverage A had an alcohol content of 5% by volume, a carbon dioxide pressure of 0.23 MPa, a DMS content of 10 ppb, and an MBT content of 3 ppt.
この発酵麦芽飲料Aに、DMS及びMBTを、飲料中の濃度が表1〜2に記載の濃度となるようにそれぞれ添加して発酵麦芽飲料B〜Jを得た。 To this fermented malt beverage A, DMS and MBT were added so that the concentrations in the beverage would be the concentrations shown in Tables 1 and 2, and fermented malt beverages B to J were obtained.
6名の専門パネルにより、発酵麦芽飲料B〜Jの飲み応えについて、発酵麦芽飲料Aを対照とした官能評価を行った。具体的には、各発酵麦芽飲料の飲み応えを、対照サンプル(発酵麦芽飲料A)を3点とし、1点が対照サンプルに比べて非常に弱く感じる、2点が対照サンプルに比べて弱く感じる、3点が対照サンプルと同等に感じる、4点が対照サンプルに比べて強く感じる、5点が対照サンプルに比べて非常に強く感じる、とする5段階で、ブラインドで評価した。6名のパネルの評点の平均値が3.5以上の場合に、飲み応えの改善効果があったと評価した。評価結果を表1〜2に示す。表中の官能評価の欄の「○」は飲み応え改善効果があったとの評価を、「×」は飲み応え改善効果がなかったとの評価をそれぞれ示す。 A sensory evaluation was performed on the fermented malt beverages B to J with a special panel of six persons, with the fermented malt beverage A as a control. Specifically, the drinking response of each fermented malt beverage is 3 points for the control sample (fermented malt beverage A), 1 point feels very weak compared to the control sample, 2 points feel weak compared to the control sample A blind evaluation was made in five stages, with 3 points feeling the same as the control sample, 4 points feeling stronger than the control sample, and 5 points feeling very strong compared to the control sample. When the average score of the panel of 6 people was 3.5 or more, it was evaluated that there was an effect of improving drinking response. The evaluation results are shown in Tables 1-2. “◯” in the column of sensory evaluation in the table indicates evaluation that there was an improvement effect on drinking response, and “×” indicates evaluation that there was no improvement effect on drinking response.
表1及び2に示すように、DMS含有量が15ppb以上、MBT含有量が5ppt以上であった発酵麦芽飲料F〜Lは、いずれも飲み応え改善効果が観察された。一方で、DMS含有量が15ppb以上ではあるものの、MBT含有量が5ppt未満であった発酵麦芽飲料C及びEは、飲み応え改善効果が観察されなかった。MBT含有量が5ppt以上ではあるものの、DMS含有量が10ppbであった発酵麦芽飲料B及びDは、MBTを添加しなかった発酵麦芽飲料Aよりも飲み応えは悪化していた。 As shown in Tables 1 and 2, all the fermented malt beverages F to L having a DMS content of 15 ppb or more and an MBT content of 5 ppt or more were observed to have an improved drinking response. On the other hand, although the DMS content was 15 ppb or more, the fermented malt beverages C and E, whose MBT content was less than 5 ppt, were not observed to have an improved drinking response. Although the MBT content was 5 ppt or more, the fermented malt beverages B and D, which had a DMS content of 10 ppb, had a worse drinking response than the fermented malt beverage A to which no MBT was added.
[実施例2]
麦芽使用比率の異なる発酵麦芽飲料にそれぞれ、DMS及びMBTを添加し、飲み応えに対する影響を調べた。
[Example 2]
DMS and MBT were respectively added to fermented malt beverages having different malt use ratios, and the influence on drinking response was examined.
麦芽の使用量を2kg、液糖の使用量を30kg(固形分75質量%)とし、麦芽使用比率を6質量%とした以外は実施例1の発酵麦芽飲料Aと同様にして、アルコール度数5容量%、炭酸ガス圧0.23MPaである発酵麦芽飲料を製造し、これにMBTとDMSをそれぞれ、飲料のMBT含有量が5ppt、DMS含有量が20ppbとなるように添加し、発酵麦芽飲料Mを製造した。 The alcohol content is 5 in the same manner as in the fermented malt beverage A of Example 1 except that the amount of malt used is 2 kg, the amount of liquid sugar used is 30 kg (solid content: 75% by mass), and the malt usage ratio is 6% by mass. A fermented malt beverage having a volume% and a carbon dioxide pressure of 0.23 MPa is produced, and MBT and DMS are added to the beverage so that the MBT content of the beverage is 5 ppt and the DMS content is 20 ppb, respectively. Manufactured.
また、麦芽の使用量を20kg、液糖の使用量を20kg(固形分75質量%)とし、大豆タンパク質は使用せず、麦芽使用比率を51質量%とした以外は実施例1の発酵麦芽飲料Aと同様にして、アルコール度数5容量%、炭酸ガス圧0.23MPaである発酵麦芽飲料を製造し、これにMBTとDMSをそれぞれ、飲料のMBT含有量が6ppt、DMS含有量が20ppbとなるように添加し、発酵麦芽飲料Nを製造した。 Further, the fermented malt beverage of Example 1 except that the amount of malt used was 20 kg, the amount of liquid sugar used was 20 kg (solid content: 75% by mass), soy protein was not used, and the malt usage ratio was 51% by mass. In the same manner as A, a fermented malt beverage having an alcohol content of 5% by volume and a carbon dioxide pressure of 0.23 MPa is produced, and MBT and DMS are respectively added to this with an MBT content of 6 ppt and a DMS content of 20 ppb. And fermented malt beverage N was produced.
実施例1で製造した発酵麦芽飲料Aを対照として実施例1と同様にして、発酵麦芽飲料M及びNの発酵麦芽飲料Fの飲み応えを官能評価した。結果を、実施例1の発酵麦芽飲料A及びFの結果と共に表3に示す。この結果、麦芽使用比率が51質量%であった発酵麦芽飲料Nでは飲み応え改善効果が観察されたが、麦芽使用比率が6質量%であった発酵麦芽飲料Mでは飲み応え改善効果が観察されなかった。 Using the fermented malt beverage A produced in Example 1 as a control, the drinking response of the fermented malt beverages M and N was subjected to sensory evaluation in the same manner as in Example 1. The results are shown in Table 3 together with the results of the fermented malt beverages A and F of Example 1. As a result, in the fermented malt beverage N in which the malt use ratio was 51% by mass, a drinking response improving effect was observed, but in the fermented malt beverage M in which the malt use rate was 6% by mass, the drinking response improving effect was observed. There wasn't.
Claims (7)
得られた発酵原料液に酵母を接種して発酵させる発酵工程と、
を有し、
ジメチルスルフィド含有量が15ppb以上であり、3−メチル−2−ブテン−1−チオール含有量が5ppt以上である発酵麦芽飲料を製造することを特徴とする、発酵麦芽飲料の製造方法。 A saccharification treatment of a mixture containing a fermentation raw material containing malt and water, and a charging step of preparing a fermentation raw material solution by boiling the obtained saccharified solution;
A fermentation process in which yeast is inoculated and fermented to the obtained fermentation raw material liquid;
Have
A method for producing a fermented malt beverage, comprising producing a fermented malt beverage having a dimethyl sulfide content of 15 ppb or more and a 3-methyl-2-butene-1-thiol content of 5 ppt or more.
ジメチルスルフィド含有量が15ppb以上及び3−メチル−2−ブテン−1−チオール含有量が5ppt以上となるように調整することを特徴とする、発酵麦芽飲料の飲み応えを改善する方法。 In order to improve the drinking response of the fermented malt beverage, the content of dimethyl sulfide and 3-methyl-2-butene-1-thiol in the beverage is
A method for improving the drinking response of a fermented malt beverage, comprising adjusting the dimethyl sulfide content to be 15 ppb or more and the 3-methyl-2-butene-1-thiol content to be 5 ppt or more.
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