JP2008136412A - Method for producing sparkling alcoholic beverage - Google Patents

Method for producing sparkling alcoholic beverage Download PDF

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JP2008136412A
JP2008136412A JP2006325382A JP2006325382A JP2008136412A JP 2008136412 A JP2008136412 A JP 2008136412A JP 2006325382 A JP2006325382 A JP 2006325382A JP 2006325382 A JP2006325382 A JP 2006325382A JP 2008136412 A JP2008136412 A JP 2008136412A
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alcoholic beverage
sparkling alcoholic
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JP4275170B2 (en
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Koichiro Takahashi
浩一郎 高橋
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Asahi Breweries Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a sparkling alcoholic beverage having an excellent flavor and foam retention without causing a production problem and to provide the sparkling alcoholic beverage produced by the production method. <P>SOLUTION: The method for producing the sparkling alcoholic beverage comprises using a protein hydrolyzate having a weight-average molecular weight of 10,000-50,000 as a part of a fermentation raw material liquid before a fermentation with yeast. The sparkling alcoholic beverage is produced by the production method. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、タンパク分解物を用いた発泡性アルコール飲料の製造方法及び該製造方法により製造した発泡性アルコール飲料に関する。   The present invention relates to a method for producing an effervescent alcoholic beverage using a proteolysate and an effervescent alcoholic beverage produced by the production method.

近年、ビールに続く新たなアルコール飲料として、米やコーンスターチ等の麦芽以外の原料を多く使用した発泡酒や、麦芽を一切使用しないビール様発泡性アルコール飲料(ビールのような風味を有する発泡性アルコール飲料)が開発された。しかしながら、発泡酒やビール様発泡性アルコール飲料は、ビールに比べ、香味や泡品質等が劣るという問題がある。特に、泡は、ビール類にとって重要な外観品質であり、泡持ちが劣ることは、消費者にとっての発泡酒等の魅力を半減させてしまうものであり、泡品質の改善が強く望まれている。   In recent years, as a new alcoholic beverage following beer, sparkling liquor using many ingredients other than malt, such as rice and corn starch, and beer-like sparkling alcoholic beverages that do not use any malt (a sparkling alcohol with a beer-like flavor Beverage) was developed. However, sparkling liquor and beer-like sparkling alcoholic beverages have a problem that flavor and foam quality are inferior to beer. In particular, foam is an important appearance quality for beers, and the poor foam retention reduces the attractiveness of happoshu and the like for consumers, and improvement of foam quality is strongly desired. .

発泡酒等の香味や泡品質等の問題を解決すべく、種々の方法が開示されている。例えば、ビールの泡は麦芽由来の泡タンパク質によるものであるため、起泡性タンパク質の欠乏を補うべく、大豆タンパクを添加することにより、泡持ちを改善する方法がある。   Various methods have been disclosed in order to solve problems such as flavor and foam quality of happoshu. For example, since beer foam is derived from malt-derived foam protein, there is a method of improving foam retention by adding soy protein in order to compensate for the lack of foaming protein.

一方、大豆タンパクの分解物を用いた方法として、例えば、(1)ビールや雑酒のような発酵アルコール飲料の製造方法において、原料の一部に小麦グルテンや大豆タンパクのようなビール酵母高資化性アミノ酸高含有蛋白原料の分解物又はその調製物を用いることにより、ビール酵母による発酵を促進して、味覚・風味を増進させ、異臭や未熟臭のない、すっきりとした味覚であり、しかもボディ感のある発酵アルコール飲料を製造する方法が開示されている(例えば、特許文献1参照。)。
その他、(2)平均分子量200〜4,000のペプチドを主発酵の初期以前の時点で発酵原料液に添加して発酵を行うことにより、従来にない香味を有するビールを製造し得ることを特徴とする、新規ビールの製造方法が開示されている(例えば、特許文献2参照。)。
特開2006−158268号公報 特許第3547532号公報
On the other hand, as a method using a degradation product of soy protein, for example, (1) In a method for producing a fermented alcoholic beverage such as beer or miscellaneous sake, beer yeast high capital such as wheat gluten or soy protein is used as part of the raw material. By using a degradation product of a protein raw material containing a high level of volatile amino acids or a preparation thereof, it promotes fermentation by brewer's yeast, enhances the taste and flavor, and has a clean taste with no off-flavors or immature odors, and A method for producing a fermented alcoholic beverage with a body feeling is disclosed (for example, see Patent Document 1).
In addition, (2) by adding a peptide having an average molecular weight of 200 to 4,000 to the fermentation raw material liquid at the time before the initial stage of the main fermentation and performing fermentation, a beer having an unprecedented flavor can be produced. The manufacturing method of the novel beer is disclosed (for example, refer patent document 2).
JP 2006-158268 A Japanese Patent No. 3547532

しかしながら、大豆タンパクをそのまま添加すると、液粘性が上がり、濾過が遅延する等の製造上の問題が引き起こされてしまう。また、大豆タンパクは溶解度が低く、利用効率が劣るという問題もある。
一方、該(1)及び(2)の方法により、香味の問題は解決され、かつ、液粘性が下がり、濾過遅延等の問題も解決されるが、特許文献1及び2には、泡品質の向上については一切記載がない。
However, if soy protein is added as it is, the viscosity of the liquid increases, causing problems in production such as delayed filtration. In addition, soy protein has a problem of low solubility and poor utilization efficiency.
On the other hand, the method of (1) and (2) solves the problem of flavor and lowers the viscosity of the liquid and solves problems such as filtration delay. There is no mention of improvement.

本発明は、製造上の問題を引き起こすことなく、香味、泡持ちがすぐれた発泡性アルコール飲料の製造方法、及び該製造方法により製造した発泡性アルコール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 producing a sparkling alcoholic beverage having excellent flavor and foam without causing problems in production, and a sparkling alcoholic beverage produced by the manufacturing 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、大豆タンパクの分解度を指標に検討し、発酵前の発酵原料液の原料の一つとして、適当な大きさのタンパク分解物を用いることにより、製造上の問題を引き起こすことなく、香味、泡持ちがすぐれた発泡性アルコール飲料が製造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-mentioned problems, the present inventors have studied using the degree of degradation of soybean protein as an index, and as a raw material for fermentation raw material liquid before fermentation, a proteolytic product of an appropriate size is used. By using it, it was found that a sparkling alcoholic beverage excellent in flavor and foam could be produced without causing problems in production, and the present invention was completed.

すなわち、発泡性アルコール飲料の製造方法において、重量平均分子量10,000〜50,000のタンパク分解物を、酵母による発酵前の発酵原料液の原料の一つとして用いること、を特徴とする発泡性アルコール飲料の製造方法を提供するものである。
また、前記タンパク分解物を、発酵原料液の煮沸処理前又は煮沸処理中に混合することを特徴とする、発泡性アルコール飲料の製造方法を提供するものである。
また、本発明は、前記タンパク分解物の重量平均分子量が13,000〜43,000である、発泡性アルコール飲料の製造方法を提供するものである。
また、本発明は、前記タンパク分解物の重量平均分子量が15,000〜35,000である、発泡性アルコール飲料の製造方法を提供するものである。
また、本発明は、前記タンパク分解物が、大豆タンパク分解物である、発泡性アルコール飲料の製造方法を提供するものである。
また、本発明は、前記タンパク分解物の混合が、液糖、窒素源、ホップ、色素、及び温水からなる群より選ばれる1以上と共になされるものである、発泡性アルコール飲料の製造方法を提供するものである。
また、本発明は、前記いずれか記載の発泡性アルコール飲料の製造方法によって製造された発泡性アルコール飲料を提供するものである。
That is, in the method for producing an effervescent alcoholic beverage, a proteolytic product having a weight average molecular weight of 10,000 to 50,000 is used as one of raw materials of a fermentation raw material liquid before fermentation with yeast. A method for producing an alcoholic beverage is provided.
Moreover, the said proteolysate is mixed before the boiling process of a fermentation raw material liquid, or during a boiling process, The manufacturing method of a sparkling alcoholic beverage characterized by the above-mentioned is provided.
Moreover, this invention provides the manufacturing method of a sparkling alcoholic beverage whose weight average molecular weights of the said protein degradation product are 13,000-43,000.
Moreover, this invention provides the manufacturing method of a sparkling alcoholic beverage whose weight average molecular weights of the said protein degradation product are 15,000-35,000.
Moreover, this invention provides the manufacturing method of a sparkling alcoholic beverage whose said protein degradation product is a soybean protein degradation product.
The present invention also provides a method for producing a sparkling alcoholic beverage, wherein the proteolytic product is mixed with one or more selected from the group consisting of liquid sugar, nitrogen source, hops, pigments, and hot water. To do.
Moreover, this invention provides the sparkling alcoholic beverage manufactured by the manufacturing method of one of the said sparkling alcoholic beverages.

本発明により、泡持ちがすぐれた発泡性アルコール飲料を製造することができる。泡持ちは、消費者が発泡性アルコール飲料を選択する上で重要な要素であり、本発明に係る製造方法により製造された発泡性アルコール飲料には、外観品質上の優位性がもたらされると期待される。
また、液粘性が下がるため、濾過遅延等の製造上の問題が解決され、かつ、過度なエステル類等の香味成分の生成が抑制される結果、本発明に係る製造方法により製造された発泡性アルコール飲料の嗜好性が向上する。
予め、泡持ちに最適な大きさのタンパク分解物を用意し、これを発酵原料液に混合することにより、泡持ちや香味のよい発泡性アルコール飲料を再現性良く製造することができるため、製品の品質管理上も好ましい。
さらに、タンパク分解物の利用効率改善の結果、製造コストの改善も期待される。
According to the present invention, it is possible to produce a sparkling alcoholic beverage with excellent foam retention. Foaming is an important factor for consumers to select a sparkling alcoholic beverage, and it is expected that the sparkling alcoholic beverage produced by the production method according to the present invention will have a superior appearance quality. Is done.
In addition, since the liquid viscosity is lowered, production problems such as filtration delay are solved, and the production of excessive flavor components such as esters is suppressed. As a result, the foamability produced by the production method according to the present invention The preference of alcoholic beverages is improved.
Providing a proteolysate of the optimum size for foam retention in advance and mixing it with the fermentation raw material liquid enables us to produce foamable alcoholic beverages with good foam retention and flavor with good reproducibility. It is also preferable for quality control.
Furthermore, as a result of improving the utilization efficiency of protein degradation products, an improvement in production cost is also expected.

本発明における発泡性アルコール飲料とは、酒税法上の分類にとらわれず、炭酸ガスによる発泡性を有し、かつアルコールを含有する飲料を意味する。したがって、発泡性アルコール飲料には、ビール、発泡酒、麦芽を使用しない発泡性アルコール飲料等が含まれる。このうち、発泡酒又は麦芽を使用しない発泡性アルコール飲料が好ましい。   The effervescent alcoholic beverage in the present invention means a beverage that has effervescence by carbon dioxide gas and contains alcohol, regardless of the classification under the liquor tax law. Therefore, sparkling alcoholic beverages include beer, sparkling alcohol, sparkling alcoholic beverages that do not use malt. Of these, sparkling alcoholic beverages that do not use sparkling liquor or malt are preferred.

まず、一般的な発泡性アルコール飲料の製造工程を示す。麦芽を原料として使用する場合と、麦芽を原料として使用しない場合を、それぞれ分けて示す。   First, the manufacturing process of a general sparkling alcoholic beverage will be shown. The case where malt is used as a raw material and the case where malt is not used as a raw material are shown separately.

ビールや発泡酒等の麦芽を原料として使用する発泡性アルコール飲料は、次の工程で製造される。まず、主原料である麦芽の破砕物と、副原料である米やコーンスターチ等の澱粉質に、温水を加えて混合・加温し、主に麦芽の酵素を利用して、澱粉質を糖化させる。この糖化液を濾過して得られた濾液にホップを加え、煮沸する。ホップは煮沸開始から煮沸終了前であればどの段階で混合してもよい。煮沸後、ワールプールと呼ばれる槽でホップ粕等の沈殿物を除去し、プレートクーラーにより適切な発酵温度まで冷却する。冷却した濾液に酵母を接種して、発酵を行う。次いで得られた発酵液を熟成させた後、濾過により酵母及びタンパク質等を除去して、目的の発泡性アルコール飲料を得る。   A sparkling alcoholic beverage that uses malt such as beer or sparkling liquor as a raw material is manufactured in the following steps. First, warm water is added to the crushed material of malt, which is the main ingredient, and starch, such as rice and corn starch, which is the auxiliary ingredient, mixed and heated, and the starch is saccharified mainly using malt enzymes. . Hops are added to the filtrate obtained by filtering this saccharified solution and boiled. Hops may be mixed at any stage from the start of boiling to the end of boiling. After boiling, precipitates such as hop cake are removed in a tank called a whirlpool and cooled to an appropriate fermentation temperature with a plate cooler. The cooled filtrate is inoculated with yeast and fermented. Next, after aging the obtained fermentation broth, yeast and proteins are removed by filtration to obtain the desired sparkling alcoholic beverage.

麦芽を使用しない発泡性アルコール飲料を製造する場合には、炭素源を含有する液糖、麦又は麦芽以外のアミノ酸含有材料としての窒素源、ホップ、色素等を、温水と共に混合し、液糖溶液を調製する。該液糖溶液を、麦芽を原料として使用する発泡性アルコール飲料の製造工程と同様に、煮沸し、ホップ粕等の沈殿物を除去して冷却後、酵母を接種して発酵させ、濾過することにより、目的の発泡性アルコール飲料を得る。ホップは煮沸開始前ではなく、煮沸中に、該液糖溶液に混合してもよい。   When producing an effervescent alcoholic beverage that does not use malt, liquid sugar containing a carbon source, nitrogen source as an amino acid-containing material other than wheat or malt, hops, pigments, etc. are mixed with warm water, and a liquid sugar solution To prepare. The liquid sugar solution is boiled in the same manner as in the production process of an effervescent alcoholic beverage using malt as a raw material, and after removing precipitates such as hop koji and cooling, inoculating and fermenting with yeast, filtering. Thus, the desired sparkling alcoholic beverage is obtained. Hops may be mixed with the liquid sugar solution during boiling, not before the start of boiling.

本発明において用いられる麦芽の破砕物、米やコーンスターチ等の澱粉質、ホップ、炭素源を含有する液糖、麦又は麦芽以外のアミノ酸含有材料としての窒素源、色素等の原料は、特に限定されるものではなく、通常発泡性アルコール飲料を製造する場合に用いられるものを、通常用いられる量で用いることができる。   Raw materials such as crushed malt used in the present invention, starch such as rice and corn starch, hops, liquid sugar containing carbon source, nitrogen source as amino acid-containing material other than wheat or malt, pigments and the like are particularly limited. What is normally used when manufacturing an effervescent alcoholic beverage can be used in the quantity normally used.

本発明において用いられるタンパク分解物は、植物由来、動物由来又は微生物由来のいずれのタンパク分解物でもよいが、ことに大豆タンパク分解物が好ましい。大豆は非常に優れた栄養的性質を有しており、消化吸収性も良いため、近年高まっている消費者の健康志向に添うためである。   The proteolysate used in the present invention may be any of a plant-derived, animal-derived or microorganism-derived protein-degraded product, and a soybean protein-degraded product is particularly preferable. This is because soybean has very excellent nutritional properties and has good digestibility, so that it can meet the increasing consumer health orientation in recent years.

また、本発明において用いられるタンパク分解物は、原料となる植物等の組織や培養液から、抽出・精製分離後、分解することにより得られたものを用いることができる。例えば、大豆タンパク分解物は、大豆を脱脂した脱脂大豆を水抽出して酸沈殿させ、生じた分離大豆タンパクカードを調製し、分解することにより得ることができる。該分解方法はタンパク質を部分分解し得る方法であれば特に限定されるものではない。例えば、熱や圧力による分解、酸やアルカリによる分解、酵素による分解がある。簡便であり、かつ、工程制御しやすいため、酵素による分解が好ましい。   The proteolysate used in the present invention may be a product obtained by decomposing after extraction / purification / separation from a tissue such as a plant or a culture solution as a raw material. For example, a soybean protein degradation product can be obtained by water-extracting defatted soybean obtained by defatting soybean, acid-precipitating it, preparing a separated soybean protein curd, and decomposing it. The degradation method is not particularly limited as long as it is a method capable of partially degrading proteins. For example, there are decomposition by heat and pressure, decomposition by acid and alkali, and decomposition by enzyme. Degradation with an enzyme is preferable because it is simple and easy to control the process.

該酵素は、タンパク質分解酵素であれば、特に限定されるものではない。市販されているタンパク質分解酵素のうち、いずれの酵素を用いても良く、またこれらを組み合わせて用いることもできる。エキソ型プロテアーゼ活性の高い酵素は、短鎖ペプチドや遊離アミノ酸を多く産生するため、タンパク質を部分分解するためには、エキソ型プロテアーゼ活性の高い酵素よりも、エンド型プロテアーゼ活性の高い酵素の方が好ましい。   The enzyme is not particularly limited as long as it is a proteolytic enzyme. Any commercially available proteolytic enzyme may be used, or a combination thereof may be used. Enzymes with high exo-protease activity produce a large amount of short-chain peptides and free amino acids. Therefore, enzymes with high endo-type protease activity are better than enzymes with high exo-protease activity to partially degrade proteins. preferable.

本発明において用いられる重量平均分子量10,000〜50,000のタンパク分解物は、上記方法により得られる。上記方法により得られたタンパク分解物が、重量平均分子量10,000〜50,000の範囲にない場合は、タンパク分解物を大きさにより分離し、重量平均分子量10,000〜50,000の大きさのタンパク分解物を精製することにより、得ることができる。該分離方法は、タンパク分解物を大きさにより分離できる方法であれば、特に限定されるものではない。例えば、ゲル透過クロマトグラフィー法、濾過法、電気泳動法、又は遠心分離法により、大きさの混在するタンパク分解物から、目的の大きさのタンパク分解物のみを単離精製することができる。   The proteolysate having a weight average molecular weight of 10,000 to 50,000 used in the present invention is obtained by the above method. When the proteolysate obtained by the above method is not in the range of weight average molecular weight of 10,000 to 50,000, the proteolysate is separated according to size, and the weight average molecular weight of 10,000 to 50,000 is large. This can be obtained by purifying the proteolytic product. The separation method is not particularly limited as long as it is a method capable of separating the proteolysate by size. For example, only a target protein degradation product can be isolated and purified from a protein degradation product having a mixed size by gel permeation chromatography, filtration, electrophoresis, or centrifugation.

さらに、本発明において用いられるタンパク分解物は、重量平均分子量10,000〜50,000のものであれば、どのような大きさのものでもよい。重量平均分子量が10,000未満のタンパク分解物を用いると、泡持ち効果が低く、かつ、エステル類が過度に合成されるため、官能上、好ましくない。一方、重量平均分子量50,000超のタンパク分解物を用いると、液粘性が上がり、発酵後の濾過や出荷のための瓶詰工程が遅延するという製造上の問題が生ずる。特に、重量平均分子量が13,000〜43,000のタンパク分解物が好ましく、重量平均分子量が15,000〜35,000のタンパク分解物がより好ましい。泡持ちが顕著に改善され、かつ、香味成分の過剰な合成が抑制されることにより嗜好性が向上するためである。   Furthermore, the proteolysate used in the present invention may have any size as long as it has a weight average molecular weight of 10,000 to 50,000. Use of a proteolysate having a weight average molecular weight of less than 10,000 is not functionally preferable because the foam retention effect is low and esters are excessively synthesized. On the other hand, when a protein degradation product having a weight average molecular weight of more than 50,000 is used, the viscosity of the liquid rises, resulting in a manufacturing problem in that the post-fermentation filtration and the bottling process for shipping are delayed. In particular, a proteolysate having a weight average molecular weight of 13,000 to 43,000 is preferable, and a proteolysate having a weight average molecular weight of 15,000 to 35,000 is more preferable. This is because the foaming property is remarkably improved, and the palatability is improved by suppressing excessive synthesis of flavor components.

本発明において用いられる酵母による発酵前の発酵原料液は、上記発泡性アルコール飲料の製造工程において、煮沸処理がなされる溶液に、タンパク分解物が混合されたものである。すなわち、麦芽を原料として使用する発泡性アルコール飲料の場合には、糖化液を濾過して得られた濾液に、また、麦芽を使用しない発泡性アルコール飲料の場合には、液糖等を混合した液糖溶液に、それぞれタンパク分解物を混合したものである。
タンパク分解物は、煮沸前から発酵前の、いずれの段階において発酵原料液に混合してもよく、炭素源を含有する液糖、窒素源、ホップ、色素及び温水等からなる群より選ばれる1以上と共に、混合してもよい。例えば、ホップを煮沸途中に添加する場合には、ホップと共にタンパク分解物を混合してもよい。
The fermentation raw material liquid before fermentation by yeast used in the present invention is a mixture obtained by mixing a proteolytic product with a solution that is boiled in the production process of the sparkling alcoholic beverage. That is, in the case of an effervescent alcoholic beverage that uses malt as a raw material, in the case of an effervescent alcoholic beverage that does not use malt, liquid sugar or the like was mixed with the filtrate obtained by filtering the saccharified solution. Proteolytic products are mixed with the liquid sugar solution.
The proteolysate may be mixed with the fermentation raw material liquid at any stage before boiling and before fermentation, and is selected from the group consisting of liquid sugar containing a carbon source, nitrogen source, hops, pigment, hot water, and the like 1 You may mix with the above. For example, when adding a hop in the middle of boiling, you may mix a protein degradation product with a hop.

発酵末期以降に混合すると、混合したタンパク分解物により沈殿や濁りが生じてしまうため、好ましくない。煮沸時の加熱によりタンパク分解物が若干変性され、沈殿や濁りを生ずるタンパク質を沈降除去できることから、泡持ち向上のために混合するタンパク分解物は、発酵原料液の煮沸処理前又は煮沸処理中に混合することが好ましい。   Mixing after the end of fermentation is not preferable because precipitation and turbidity are caused by the mixed protein degradation product. Proteolysis products are slightly denatured by heating during boiling, and proteins that cause precipitation or turbidity can be removed by sedimentation.Proteolysis products to be mixed to improve foam retention can be used before or during the boiling treatment of the fermentation raw material liquid. It is preferable to mix.

発酵原料液の一部として用いるタンパク分解物量は、特に限定されるものではないが、発酵原料液に0.01%(重量/体積)〜3%(重量/体積)が好ましい。   The amount of the proteolysate used as a part of the fermentation raw material liquid is not particularly limited, but is preferably 0.01% (weight / volume) to 3% (weight / volume) in the fermentation raw material liquid.

より具体的には、例えば、麦芽を原料として使用する発泡性アルコール飲料の場合、通常の製造工程において、糖化液を濾過して得られた濾液の煮沸開始時に大豆タンパク分解物を混合し、95〜105℃で煮沸する。麦芽を使用しない発泡性アルコール飲料の場合には、煮沸釜に必要量の液糖、窒素源、カラメル、ホップ及び温水と共に大豆タンパク分解物を混合し、同様に煮沸する。煮沸時間は特に限定されるものではないが、60分〜100分が好ましい。   More specifically, for example, in the case of an effervescent alcoholic beverage using malt as a raw material, the soy protein degradation product is mixed at the start of boiling of the filtrate obtained by filtering the saccharified solution in a normal production process, and 95 Boil at ~ 105 ° C. In the case of an effervescent alcoholic beverage that does not use malt, a soybean protein degradation product is mixed with a required amount of liquid sugar, nitrogen source, caramel, hops and hot water in a boiling kettle and boiled in the same manner. Although boiling time is not specifically limited, 60 minutes-100 minutes are preferable.

煮沸処理後、発酵原料液からホップ粕等の沈殿物を除去して冷却し、酵母を接種して発酵・熟成させ、濾過により酵母及びタンパク質等を除去することにより、目的の発泡性アルコール飲料を得ることができる。沈殿物の除去、冷却、発酵等の方法は、特に限定されるものではなく、通常発泡性アルコール飲料を製造する場合に用いられる方法で行うことができる。発酵に用いられる酵母も、特に限定されるものではないが、安全性、入手の容易さ等からサッカロマイセス属に属するものが好ましい。   After boiling treatment, remove the precipitate such as hop koji from the fermentation raw material liquid, cool it, inoculate the yeast, ferment and mature, and remove the yeast and protein by filtration to obtain the desired sparkling alcoholic beverage Obtainable. The method of removing the precipitate, cooling, fermentation, etc. is not particularly limited, and can be carried out by a method usually used for producing a sparkling alcoholic beverage. The yeast used for fermentation is not particularly limited, but yeast belonging to the genus Saccharomyces is preferable from the viewpoint of safety, availability and the like.

次に分析例、試験例を示して本発明をさらに詳細に説明するが、本発明は以下の分析例、試験例に限定されるものではない。なお、本発明は麦芽を原料として使用しない場合に限定されず、麦芽を原料として使用する場合にも該当する。   Next, although an analysis example and a test example are shown and this invention is demonstrated further in detail, this invention is not limited to the following analysis examples and test examples. In addition, this invention is not limited to when malt is not used as a raw material, It corresponds also when using malt as a raw material.

(分析例)
50mMリン酸緩衝液(1%(重量/体積)SDS、1.2%(重量/体積)NaCl、pH7.0 )を用いて希釈調整した大豆タンパク分解物溶液を、10分間超音波処理を行った後、0.2μmフィルターを用いて濾過した。得られた濾液を、TSK G3000SWXLカラム(東ソー社製)に通し、上記リン酸緩衝液を用いて大豆タンパク分解物を溶出した。大豆タンパク分解物の検出は220nmの吸光度を測定して行った。これにより、各画分に分離精製されたタンパク分解物の重量平均分子量を、GPCソフトウェア(東ソー社製)を使用して得られたチャートから算出した。分子量マーカーは、670,000(Thyrogloblin、和光純薬工業)、67,000(Albumin、SIGMA)、20,150(Trypsin inhibitor from Glycine max ; soybean、SIGMA)、5,807(Insulin、SIGMA)、1,627(Neurotensin、SIGMA)、426(Leupeptin、SIGMA)を用いた。
(Analysis example)
A soybean protein degradation product solution diluted with 50 mM phosphate buffer (1% (weight / volume) SDS, 1.2% (weight / volume) NaCl, pH 7.0) was subjected to ultrasonic treatment for 10 minutes. And then filtered using a 0.2 μm filter. The obtained filtrate was passed through a TSK G3000SWXL column (manufactured by Tosoh Corporation), and the soy proteolysate was eluted using the phosphate buffer. The soy protein degradation product was detected by measuring the absorbance at 220 nm. Thereby, the weight average molecular weight of the proteolysate separated and purified in each fraction was calculated from a chart obtained using GPC software (manufactured by Tosoh Corporation). Molecular weight markers are 670,000 (Thyrogloblin, Wako Pure Chemical Industries), 67,000 (Albumin, SIGMA), 20,150 (Trypsin inhibitor from Glycine max; soybean, SIGMA), 5,807 (Insulin, SIGMA), 1 , 627 (Neurotensin, SIGMA), 426 (Leupeptin, SIGMA).

(試験例1)
エンドプロテアーゼ活性を有する酵素の添加量と反応時間を変化させ、重量平均分子量が、約7,000、約13,000、約25,000、約43,000、及び約55,000の大豆タンパク分解物を得た。
(Test Example 1)
Soy proteolysis with weight average molecular weights of about 7,000, about 13,000, about 25,000, about 43,000, and about 55,000 by varying the amount of enzyme having endoprotease activity and reaction time I got a thing.

液糖40kg、酵母エキス0.5kg、カラメル0.2kg、ホップ0.02kg、及び上記方法で得た大豆タンパク分解物0.5kgを混合し、温水を約160L加えることにより、約200Lの発酵原料液を調整した。該発酵原料液を100℃で90分間煮沸した後、ワールプールでホップ粕を除去した。除去後の発酵原料液約180L(糖度14%)に温水20Lを加え、糖度12.6%に調製した後、プレートクーラーにより5℃まで冷却して、冷却した発酵原料液約170リットルを得た。該冷却済発酵原料液を発酵タンクに移し、液汁1mlあたり25×106個の泥状酵母を接種し、10℃で168時間発酵を行った。得られた発酵液を、−1℃で7日間熟成(後発酵)させた。得られた発酵液をキャンドルフィルターを用いて珪藻土濾過を行い、酵母及びタンパク等を除去し、目的の発泡性アルコール飲料(アルコール度5%、麦芽使用比率0%)を得た。 Mixing 40 kg of liquid sugar, 0.5 kg of yeast extract, 0.2 kg of caramel, 0.02 kg of hops, and 0.5 kg of soybean protein degradation product obtained by the above method, and adding about 160 L of warm water, about 200 L of fermentation raw material The liquid was adjusted. The fermentation raw material liquid was boiled at 100 ° C. for 90 minutes, and then hop koji was removed with a whirlpool. After adding 20 L of warm water to about 180 L of fermentation raw material liquid (sugar content 14%) after the removal to prepare a sugar content of 12.6%, the plate was cooled to 5 ° C. with a plate cooler to obtain about 170 liters of cooled fermentation raw material liquid. . The cooled fermentation raw material liquid was transferred to a fermentation tank, inoculated with 25 × 10 6 muddy yeast per 1 ml of juice, and fermented at 10 ° C. for 168 hours. The obtained fermentation broth was aged (post-fermented) for 7 days at -1 ° C. The obtained fermented liquor was subjected to diatomaceous earth filtration using a candle filter to remove yeast, protein, and the like, and the intended effervescent alcoholic beverage (alcohol content 5%, malt use ratio 0%) was obtained.

得られた5つの発泡性アルコール飲料の物理化学分析、官能検査、及び珪藻土濾過試験を行った。表1は物理化学分析の結果を、表2は官能検査の結果を、表3は珪藻土濾過試験の結果をそれぞれ示したものである。
発泡性アルコール飲料の物理化学分析は、ASBC(American Society of Brewing Chemists)及びEBC(European Brewery Convention)の両組織に採用されており、ビール分析の国際基準とされている分析法に準じて行った(ビール酒造組合著、「BCOJビール分析法」1996年)。具体的には、各発泡性アルコール飲料のNIBEM値と粘度を測定し、3種の香味成分(酢酸エチル、イソアミルアルコール、βフェネチルアルコール)を定量した。NIBEM値は、注がれた泡の崩壊速度を電気伝導度で測定したものであり、ビール等の泡持ち評価に一般的に用いられているものである。
官能検査は、やはりビール官能評価の国際基準であるASBC及びEBCの両組織に採用されている官能評価法に準じて行った(ビール酒造組合著、「BCOJ官能評価法」2002年)。具体的には、ビール醸造技術者10名のパネリストで行い、味感、ビールらしい香味(ビールテイスト)や泡の質感について5段階で評価した。
珪藻土濾過試験は、発泡性アルコール飲料を、キャンドル型システムを用いて珪藻土濾過をした場合の、キャンドルフィルターの差圧上昇度合いを測定することにより行った。
The obtained five sparkling alcoholic beverages were subjected to physicochemical analysis, sensory test, and diatomaceous earth filtration test. Table 1 shows the results of the physicochemical analysis, Table 2 shows the results of the sensory test, and Table 3 shows the results of the diatomite filtration test.
Physicochemical analysis of sparkling alcoholic beverages has been adopted by both organizations of the American Society of Brewing Chemists (ASBC) and the European Brewery Convention (EBC), and was performed in accordance with the analysis method that is the international standard for beer analysis. (Brew Brewery Association, "BCOJ Beer Analysis Method" 1996). Specifically, the NIBEM value and viscosity of each effervescent alcoholic beverage were measured, and three flavor components (ethyl acetate, isoamyl alcohol, β-phenethyl alcohol) were quantified. The NIBEM value is a value obtained by measuring the collapse rate of the poured foam by electric conductivity, and is generally used for foam evaluation of beer and the like.
The sensory test was carried out in accordance with the sensory evaluation method adopted by both the ASBC and EBC organizations, which are also international standards for beer sensory evaluation (by the Beer Brewery Association, “BCOJ Sensory Evaluation Method” 2002). Specifically, it was conducted by 10 panelists of beer brewing engineers, and the taste, beer-like flavor (beer taste), and foam texture were evaluated in five stages.
The diatomaceous earth filtration test was conducted by measuring the degree of increase in the differential pressure of the candle filter when the sparkling alcoholic beverage was subjected to diatomaceous earth filtration using a candle type system.

Figure 2008136412
Figure 2008136412

物理化学分析結果より、用いた大豆タンパク分解物の重量平均分子量が大きくなるほど、泡持ちが改善され、酢酸エチル等の香味成分が減少することが分かった。特に、重量平均分子量が約13,000以上の大豆タンパク分解物を用いた発泡性アルコール飲料において香味成分が顕著に減少されており、重量平均分子量が約25,000以上の大豆タンパク分解物を用いた発泡性アルコール飲料において泡持ちが顕著に改善されていることが明らかである。一方、粘度に関しては、重量平均分子量が約55,000の大豆タンパク分解物を用いた発泡性アルコール飲料では、重量平均分子量が約43,000以下の大豆タンパク分解物を用いた発泡性アルコール飲料と比較して、急激に高くなっていることが分かった。   From the physicochemical analysis results, it was found that the higher the weight average molecular weight of the soy protein degradation product used, the better the foam retention and the lower the flavor components such as ethyl acetate. In particular, flavor components are significantly reduced in a sparkling alcoholic beverage using a soy protein hydrolyzate having a weight average molecular weight of about 13,000 or more, and a soy protein hydrolyzate having a weight average molecular weight of about 25,000 or more is used. It is clear that the foam retention is significantly improved in the sparkling alcoholic beverage. On the other hand, regarding the viscosity, the sparkling alcoholic beverage using the soy protein hydrolyzate having a weight average molecular weight of about 55,000 and the sparkling alcoholic beverage using the soy protein hydrolyzate having a weight average molecular weight of about 43,000 or less and In comparison, it turned out to be abruptly higher.

Figure 2008136412
Figure 2008136412

官能検査の結果から、重量平均分子量が約7,000の大豆タンパク分解物を用いた発泡性アルコール飲料は、エステル(香味成分)が強く、官能上好ましくないが、重量平均分子量が約13,000以上の大豆タンパク分解物を用いた発泡性アルコール飲料は、良好な官能特性を示し、嗜好性が向上されていることが明らかである。   From the results of the sensory test, the effervescent alcoholic beverage using the soybean protein degradation product having a weight average molecular weight of about 7,000 has a strong ester (flavoring component) and is not preferred in terms of functionality, but the weight average molecular weight is about 13,000. It is clear that the effervescent alcoholic beverage using the soybean protein degradation product described above exhibits good sensory characteristics and has improved palatability.

Figure 2008136412
Figure 2008136412

珪藻土濾過試験の結果、重量平均分子量が約55,000の大豆タンパク分解物を用いた発泡性アルコール飲料では、急激な差圧上昇が認められ、濾過が不能となり、濾過量が大幅に減少することが認められた。したがって、重量平均分子量が50,000超の大豆タンパク分解物を用いると、濾過遅延等の製造上の問題が生ずることが明らかである。   As a result of the diatomite filtration test, in the effervescent alcoholic beverage using the soybean protein degradation product having a weight average molecular weight of about 55,000, a sudden increase in the differential pressure is recognized, the filtration becomes impossible, and the filtration amount is greatly reduced. Was recognized. Therefore, it is clear that production problems such as filtration delay occur when a soybean protein degradation product having a weight average molecular weight of more than 50,000 is used.

以上の試験例の結果から、重量平均分子量が10,000〜50,000程度の大きさの大豆タンパク分解物を用いることにより、濾過遅延等の製造上の問題を引き起こすことなく、泡持ち、香味のよい発泡性アルコール飲料を製造することができることが明らかである。特に、重量平均分子量が15,000〜35,000程度の大きさの大豆タンパク分解物を用いることにより、発泡性アルコール飲料の泡持ちと香味の両方が、顕著に改善されることがわかる。   From the results of the above test examples, by using a soybean protein hydrolyzate having a weight average molecular weight of about 10,000 to 50,000, it has foam and flavor without causing problems in production such as filtration delay. It is clear that a good sparkling alcoholic beverage can be produced. In particular, it can be seen that by using a soybean protein degradation product having a weight average molecular weight of about 15,000 to 35,000, both foam retention and flavor of the sparkling alcoholic beverage are remarkably improved.

(試験例2)
次に、重量平均分子量が約25,000の大豆タンパク分解物を混合する時期を、煮沸開始時、煮沸中(煮沸終了30分前)、及び、発酵終了時の、それぞれにおいてする以外は、試験例1と同様にして、発泡性アルコール飲料を得た。
(Test Example 2)
Next, a test was conducted except that the time when the soy protein hydrolyzate having a weight average molecular weight of about 25,000 was mixed was at the start of boiling, during boiling (30 minutes before the end of boiling), and at the end of fermentation. In the same manner as in Example 1, a sparkling alcoholic beverage was obtained.

得られた3つの発泡性アルコール飲料の、物理化学的分析を行った。それぞれの分析は、瓶詰めした最終製品を用いて実施した。具体的には、各発泡性アルコール飲料のNIBEM値と混濁度(EBC)を測定した。測定結果は表4のようになった。   The obtained three sparkling alcoholic beverages were subjected to physicochemical analysis. Each analysis was performed using the final bottled product. Specifically, the NIBEM value and turbidity (EBC) of each sparkling alcoholic beverage were measured. The measurement results are shown in Table 4.

Figure 2008136412
Figure 2008136412

試験例2の結果から、大豆タンパク分解物を、煮沸前又は煮沸中に発酵原料液に混合したほうが、発酵終了後に混合するよりも、泡持ちの良好な発泡性アルコール飲料を得ることができることがわかった。
また、大豆タンパク分解物を発酵終了後に混合した場合の発泡性アルコール飲料は、煮沸処理前又は煮沸処理中に混合したものと比べ、混濁度が高いことがわかった。混濁度が高い、すなわち、濁りのある発泡性アルコール飲料は、外観品質が劣り、好ましくない。したがって、タンパク分解物は、発酵前、特に、発酵原料液の煮沸処理前又は煮沸処理中に混合するほうが好ましいことが明らかである。
From the results of Test Example 2, it is possible to obtain a foaming alcoholic beverage with good foaming properties by mixing the soy proteolysate with the fermentation raw material liquid before or during boiling, rather than mixing it after the end of fermentation. all right.
Moreover, it turned out that the effervescent alcoholic beverage at the time of mixing a soybean protein degradation product after completion | finish of fermentation has high turbidity compared with what was mixed before the boiling process or during the boiling process. A sparkling alcoholic beverage having high turbidity, i.e., turbidity, is unfavorable because of poor appearance quality. Therefore, it is clear that it is preferable to mix the proteolysate before fermentation, particularly before or during the boiling treatment of the fermentation raw material liquid.

本発明に係る発泡性アルコール飲料の製造方法は、製造上の問題を引き起こすことなく、香味、泡持ちがすぐれた発泡性アルコール飲料を提供することができるため、発泡性アルコール飲料の製造分野で利用が可能である。   The method for producing an effervescent alcoholic beverage according to the present invention can provide an effervescent alcoholic beverage with excellent flavor and foam without causing problems in production, and is used in the field of producing an effervescent alcoholic beverage. Is possible.

麦芽を使用しない発泡性アルコール飲料の製造工程の概略を示したものである。The outline of the manufacturing process of the effervescent alcoholic beverage which does not use malt is shown.

Claims (7)

発泡性アルコール飲料の製造方法において、重量平均分子量10,000〜50,000のタンパク分解物を、酵母による発酵前の発酵原料液の原料の一つとして用いること、を特徴とする発泡性アルコール飲料の製造方法。   In the method for producing a sparkling alcoholic beverage, a proteolysate having a weight average molecular weight of 10,000 to 50,000 is used as one of the raw materials of the fermentation raw material liquid before fermentation with yeast. Manufacturing method. 前記タンパク分解物を、発酵原料液の煮沸処理前又は煮沸処理中に混合することを特徴とする、請求項1記載の発泡性アルコール飲料の製造方法。   The method for producing an effervescent alcoholic beverage according to claim 1, wherein the protein degradation product is mixed before or during the boiling treatment of the fermentation raw material liquid. 前記タンパク分解物の重量平均分子量が13,000〜43,000である、請求項1又は2記載の発泡性アルコール飲料の製造方法。   The manufacturing method of the sparkling alcoholic beverage of Claim 1 or 2 whose weight average molecular weights of the said protein degradation product are 13,000-43,000. 前記タンパク分解物の重量平均分子量が15,000〜35,000である、請求項1又は2記載の発泡性アルコール飲料の製造方法。   The manufacturing method of the sparkling alcoholic beverage of Claim 1 or 2 whose weight average molecular weights of the said protein degradation product are 15,000-35,000. 前記タンパク分解物が、大豆タンパク分解物である、請求項1〜4のいずれか記載の発泡性アルコール飲料の製造方法。   The manufacturing method of the sparkling alcoholic beverage in any one of Claims 1-4 whose said protein degradation product is a soybean protein degradation product. 前記タンパク分解物の混合が、液糖、窒素源、ホップ、色素、及び温水からなる群より選ばれる1以上と共になされるものである、請求項1〜5のいずれか記載の発泡性アルコール飲料の製造方法。   The effervescent alcoholic beverage according to any one of claims 1 to 5, wherein the proteolytic product is mixed with one or more selected from the group consisting of liquid sugar, nitrogen source, hops, pigments, and hot water. Production method. 請求項1〜6のいずれか記載の発泡性アルコール飲料の製造方法によって製造された発泡性アルコール飲料。   The sparkling alcoholic beverage manufactured by the manufacturing method of the sparkling alcoholic beverage in any one of Claims 1-6.
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