JP4448911B2 - Method for producing beer, sparkling liquor or beer-like alcoholic beverage containing phosphorylated oligosaccharide - Google Patents

Method for producing beer, sparkling liquor or beer-like alcoholic beverage containing phosphorylated oligosaccharide Download PDF

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JP4448911B2
JP4448911B2 JP2005337795A JP2005337795A JP4448911B2 JP 4448911 B2 JP4448911 B2 JP 4448911B2 JP 2005337795 A JP2005337795 A JP 2005337795A JP 2005337795 A JP2005337795 A JP 2005337795A JP 4448911 B2 JP4448911 B2 JP 4448911B2
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beer
fermentation
starch
potato starch
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JP2007135545A (en
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俊夫 永島
篤 塚本
高弘 野田
勝一 齋藤
道広 福島
謙一郎 島田
直人 橋本
圭鎬 韓
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National Agriculture and Food Research Organization
Tokyo University of Agriculture
Obihiro University of Agriculture and Veterinary Medicine NUC
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National Agriculture and Food Research Organization
Tokyo University of Agriculture
Obihiro University of Agriculture and Veterinary Medicine NUC
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Description

本発明は、リン酸化オリゴ糖を含むビール、発泡酒又はビール様アルコール飲料に関し、詳細には、リンを高濃度に含む澱粉を原料として製造したビール、発泡酒又はビール様アルコール飲料に関する。 The present invention relates to beer, sparkling liquor or beer-like alcoholic beverages containing phosphorylated oligosaccharides, and in particular, to beer, sparkling liquor or beer-like alcoholic beverages produced using starch containing phosphorus in a high concentration as a raw material.

ビールの定義は、日本の酒税法によれば、(1)「麦芽、ホップ、水を原料として発酵させたもの(麦芽100%ビール)」、(2)「麦芽、ホップ、水及び米その他の政令で定める物品を原料として発酵させたもの。ただし、その原料中の当該政令で定める物品の重量の合計が、麦芽の重量の10分の5を超えないものに限る」と規定されている。ここで、「米その他の政令で定める物品」とは、米、とうもろこし、高粱、馬鈴薯、澱粉、糖類又はカラメルである。そして、上記(1)又は(2)の条件を満たすもののみがビールであり、それ以外は発泡酒に分類される。   According to the Japanese liquor tax law, the definition of beer is (1) “Mort, hops, fermented from water (malt 100% beer)”, (2) “Mort, hops, water, rice and other The product is fermented using the articles specified by the Cabinet Order as raw materials, provided that the total weight of the articles specified by the Cabinet Order in the raw materials does not exceed 5/10 of the weight of the malt. Here, “rice and other articles specified by a government ordinance” are rice, corn, Takatsuki, potato, starch, sugar, or caramel. And only the thing which satisfy | fills the said (1) or (2) conditions is beer, and others are classified into a sparkling liquor.

従って、ビールや発泡酒の原料に種々のものを用いてそれらの味や色などを変えることが可能になる。例えば、原料に各地の農産物を用いることでビールや発泡酒の個性や付加価値を付与したり、地域の特色を出すことができるようになる。その結果、地域産業の活性化にもつながる可能性がある。   Therefore, it becomes possible to change the taste, color, etc. by using various materials for beer and happoshu. For example, by using agricultural products from various locations as raw materials, it becomes possible to give individuality and added value to beer and sparkling sake, and to give local characteristics. As a result, it may lead to the activation of local industries.

また、消費者の健康志向の高まりを受けて、種々の機能を付加したビールや発泡酒が開発されている。例えば、糖質又はプリン体を削減した発泡酒が上市され、健康を気遣う消費者を中心に大きな市場を形成している。   In addition, beer and sparkling liquor with various functions have been developed in response to increasing consumer health-consciousness. For example, Happoshu with reduced sugars or purines is on the market, forming a large market centered on consumers who care about health.

更に、麦芽、大麦、小麦を原料に使用せずにビール様アルコール飲料が製造されている。例えば、炭素源を含有するシロップと、大豆又はえんどう豆より得られた窒素源と、ホップと、水を原料として発酵前液を製造し、該発酵前液に酵母を使用して発酵させるビール様アルコール飲料の製造方法において、前記シロップを馬鈴薯から得る旨が開示されている(特許文献1)。
特開2005−124591号公報
Furthermore, beer-like alcoholic beverages are produced without using malt, barley and wheat as raw materials. For example, a beer fermented using a syrup containing a carbon source, a nitrogen source obtained from soybeans or peas, hops, and water as raw materials, and fermented using yeast in the pre-fermentation solution In a method for producing a similar alcoholic beverage, it is disclosed that the syrup is obtained from potato (Patent Document 1).
JP-A-2005-124591

ビール様アルコール飲料は種々の原料を用いることができるため、機能性を付加した商品が今後も開発されることが予想される。しかしながら、ビール又は発泡酒の味や風味を好む消費者は依然として多い。そのため、ビール及び発泡酒はビール様アルコール飲料と共に今後も消費が増加していくものと考えられる。   Since various materials can be used for beer-like alcoholic beverages, it is expected that products with added functionality will be developed in the future. However, many consumers still prefer the taste and flavor of beer or happoshu. Therefore, it is considered that consumption of beer and sparkling liquor will continue to increase together with beer-like alcoholic beverages.

しかしながら、ビールや発泡酒中には、血糖値上昇を引き起こす糖質や、尿酸値上昇を引き起こすプリン体が豊富に含まれている。そのため、ビール又は発泡酒を長期間にわたり多量に摂取し続けると、肝毒性等の疾患を引き起こす恐れがある。   However, beer and happoshu are rich in carbohydrates that cause an increase in blood sugar levels and purines that cause an increase in uric acid levels. Therefore, if a large amount of beer or happoshu is ingested over a long period of time, there is a risk of causing diseases such as liver toxicity.

麦芽の代替原料のひとつとして、馬鈴薯澱粉がある。馬鈴薯は澱粉含量が約15%と高く、既に従来から馬鈴薯澱粉を分離する方法が工業的に確立しているため大量入手が容易であり、コストも安い。そのため、馬鈴薯澱粉は発酵原料に適しているといえる。また、馬鈴薯澱粉及び澱粉関連物質には種々の生理活性があることが知られている。   Potato starch is an alternative raw material for malt. Potato has a high starch content of about 15%, and since a method for separating potato starch has already been established industrially, it is easy to obtain in large quantities and is low in cost. Therefore, it can be said that potato starch is suitable as a fermentation raw material. In addition, potato starch and starch-related substances are known to have various physiological activities.

そこで、本発明は、安定感のある天然素材であって、しかも食物繊維と比類し得る生理活性を有する素材として馬鈴薯澱粉に着目し、新規な醸造酒を提供することを目的とする。   Then, this invention pays attention to potato starch as a natural material with a sense of stability, and also has the physiological activity comparable to a dietary fiber, and it aims at providing a new brew.

本発明は、リンの濃度が600ppm以上であり、平均粒径が30μm以下である馬鈴薯澱粉を原料として用い、該馬鈴薯澱粉を麦芽及び水に添加して糖化することにより糖化液を製造する糖化工程と、該糖化液に酵母を添加してアルコール発酵を行う発酵工程と、を備えるビール、発泡酒又はビール様アルコール飲料の製造方法を提供するものである。このような構成により、リン酸化オリゴ糖を200ppm以上含有するビール、発泡酒又はビール様アルコール飲料を製造することができる。 The present invention, the concentration of phosphorus Ri der than 600 ppm, an average particle diameter using a Der Ru potato starch below 30μm as a raw material, to produce the sugar solution by saccharification by adding the potato starch in malt and water The present invention provides a method for producing a beer, a sparkling liquor, or a beer-like alcoholic beverage, comprising a saccharification step and a fermentation step in which yeast is added to the saccharified solution to perform alcoholic fermentation. With such a configuration, a beer, a sparkling liquor or a beer-like alcoholic beverage containing 200 ppm or more of a phosphorylated oligosaccharide can be produced.

本発明によれば、リン酸化オリゴ糖を200ppm以上含有する醸造酒により、従来のビール等と比較して、健康志向の消費者も安心して飲用することができる。 According to the present invention, it is possible by brew containing phosphorylated oligosaccharides or 200 ppm, compared to the conventional beer or the like, and drinking with confidence consumer health-oriented.

次に、本発明の実施形態について、更に詳細に説明する。本実施形態に係る醸造酒は、既述の通り、リン酸化オリゴ糖を含有する醸造酒であって、該リン酸化オリゴ糖の濃度が200ppm以上である。   Next, embodiments of the present invention will be described in more detail. As described above, the brewed liquor according to this embodiment is a brewed liquor containing a phosphorylated oligosaccharide, and the concentration of the phosphorylated oligosaccharide is 200 ppm or more.

前記リン酸化オリゴ糖は、馬鈴薯澱粉を由来とすることが好ましい。馬鈴薯の澱粉は、他の原料由来の澱粉に比べて、リン含量が高い。例えば、代表的な澱粉であるコーンスターチのリン含量は、140ppm前後と非常に少ない。馬鈴薯澱粉には、リンが、アミロペクチン中のグルコース残基の3位と6位にエステル結合したリン酸基として存在し、馬鈴薯澱粉には、このリン酸基が他のいも類の澱粉に比べても多い。   The phosphorylated oligosaccharide is preferably derived from potato starch. Potato starch has a higher phosphorus content than starches derived from other raw materials. For example, the phosphorus content of corn starch, which is a typical starch, is as low as around 140 ppm. In potato starch, phosphorus exists as phosphate groups that are ester-linked to the 3rd and 6th positions of the glucose residue in amylopectin. In potato starch, this phosphate group is present compared to other potato starches. There are many.

さらに、馬鈴薯澱粉は、馬鈴薯の品種によって、そのリン酸含量が異なり、低リン含量の澱粉を含有する品種と高リン含量の澱粉を含有する品種とに大きく分類できる。本実施形態では、所望の濃度のリン酸化オリゴ糖を有する醸造酒を製造するためには、馬鈴薯澱粉は、そのリンの濃度が600ppm以上であることが好ましい。   Furthermore, potato starch has different phosphate contents depending on the variety of potato, and can be broadly classified into varieties containing starch having a low phosphorus content and varieties containing starch having a high phosphorus content. In the present embodiment, in order to produce a brewed liquor having a desired concentration of phosphorylated oligosaccharide, the potato starch preferably has a phosphorus concentration of 600 ppm or more.

リン濃度が600ppm以上である品種としては、例えば、とうや、ホッカイコガネ、ワセシロ、エニワ、キタアカリ、さやか、アーリースターチ、男爵薯、コナフブキ、トヨシロ、インカパープル、インカレッド、インカのめざめ、ノーザンルビーシャドークイーン及びキタムラサキ等を挙げることができる。 Examples of the varieties having a phosphorus concentration of 600 ppm or more include, for example, Toya, Scarlet moth, Waseiro, Eniwa, Kitaakari, Sayaka, Early starch, Baron candy, Konafuki, Toyoshiro, Inca purple, Inca red, Inca medusa, Northern ruby , Shadow queen And Kitamurasaki.

馬鈴薯澱粉は、常法によりリン濃度が600ppm以上である澱粉を含有する馬鈴薯から製造されたものであることができる。   The potato starch can be produced from potato containing starch having a phosphorus concentration of 600 ppm or more by a conventional method.

馬鈴薯澱粉について、粒径で分画した粒子径の異なる澱粉には、リン含量に差異があることが知られている。一般的傾向として、平均粒子径が大きいほどリン含量は低く、粒子径が小さいほどリン含量は高い。本実施形態では、リン含量が高い馬鈴薯澱粉を用いて醸造酒を製造する方がリン酸化オリゴ糖の濃度が高くなることから、澱粉として平均粒子径が小さいものを用いることが好ましい。具体的には、馬鈴薯澱粉は、その平均粒径が30μm以下、好ましくは20μm以下であることが好ましい。なお、澱粉はα化する前の澱粉であり、平均粒子径は、α化する前の澱粉についてのものである。   As for potato starch, it is known that starches having different particle sizes fractionated by particle size have different phosphorus contents. As a general trend, the larger the average particle size, the lower the phosphorus content, and the smaller the particle size, the higher the phosphorus content. In the present embodiment, it is preferable to use a starch having a small average particle size because the concentration of phosphorylated oligosaccharide increases when brewed liquor is produced using potato starch having a high phosphorus content. Specifically, the potato starch preferably has an average particle size of 30 μm or less, preferably 20 μm or less. Note that the starch is starch before being pregelatinized, and the average particle size is that of the starch before being pregelatinized.

なお、平均粒子径が30μm以下、好ましくは20μm以下である分級澱粉を用いると、原料馬鈴薯澱粉のリン濃度が600ppm未満であっても、リン濃度を600ppm以上にできる場合があり、本実施形態における「リン濃度が600ppm以上の馬鈴薯澱粉」には、分級によってリン濃度が600ppm以上になった分級馬鈴薯澱粉も含まれる。   When classified starch having an average particle size of 30 μm or less, preferably 20 μm or less is used, the phosphorus concentration may be 600 ppm or more even if the phosphorus concentration of the raw potato starch is less than 600 ppm. The “potato starch having a phosphorus concentration of 600 ppm or higher” includes classified potato starch having a phosphorus concentration of 600 ppm or higher by classification.

前記醸造酒は、麦芽の風味を楽しむという観点からは、ビール又は発泡酒であることが好ましい。但し、麦芽を一切使用せずにビール様飲料としたいわゆる「第3のビール」に、リン酸化オリゴ糖が200ppm以上含まれていてもよい。   The brewed liquor is preferably beer or sparkling liquor from the viewpoint of enjoying the flavor of malt. However, 200 ppm or more of phosphorylated oligosaccharides may be contained in the so-called “third beer” which is a beer-like beverage without using any malt.

次に、本実施形態に係る醸造酒の製造方法について説明する。本実施形態に係る醸造酒の製造方法は、既述の通り、リンの濃度が600ppm以上である馬鈴薯澱粉を原料として用いる。なお、前記馬鈴薯澱粉は、醸造酒中のリン酸化オリゴ糖含量を高める観点から、その平均粒径が30μm以下、好ましくは20μm以下のものを原料として用いてもよい。   Next, the manufacturing method of the brewed liquor which concerns on this embodiment is demonstrated. As described above, the method for producing brewed liquor according to the present embodiment uses potato starch having a phosphorus concentration of 600 ppm or more as a raw material. In addition, from the viewpoint of increasing the phosphorylated oligosaccharide content in the brewed liquor, the potato starch may have an average particle size of 30 μm or less, preferably 20 μm or less as a raw material.

まず、上記原料は加熱処理が施されα化される。α化された原料は、次に糖化処理がなされる。糖化は、例えば、50〜70℃、65〜90分の条件で行うことができる。なお、糖化温度と時間は、用いる糖化酵素の至適温度に応じて適宜設定される。   First, the raw material is subjected to a heat treatment and is α-ized. The saccharified raw material is then saccharified. Saccharification can be performed, for example, under conditions of 50 to 70 ° C. and 65 to 90 minutes. The saccharification temperature and time are appropriately set according to the optimum temperature of the saccharifying enzyme to be used.

麦芽はビール醸造又は発泡酒醸造に一般的に用いられる麦芽を使用することができ、その種類に特に制限はない。麦芽の配合量は、ビールを製造するか、発泡酒を製造するかによって適宜選択することができる。例えば、酒税法に定義するビールを製造するためには、麦芽重量が67重量%を超えるように調節される。   As the malt, malt generally used for beer brewing or happoshu brewing can be used, and the type thereof is not particularly limited. The blending amount of malt can be appropriately selected depending on whether beer is produced or happoshu is produced. For example, in order to produce beer as defined in the liquor tax law, the malt weight is adjusted to exceed 67% by weight.

原料の添加量は、麦芽の添加量に応じて適宜設定されるが、麦芽の風味を残しつつ、リン酸化オリゴ糖含量を高めるという観点からは、原料の全量を基準(100重量%)とした場合に、35〜65重量%であることがより好ましく、40〜60重量%であることが更に好ましい。 The addition amount of the raw material is appropriately set according to the addition amount of the malt. From the viewpoint of increasing the phosphorylated oligosaccharide content while leaving the flavor of the malt, the total amount of the raw material is set as the standard (100% by weight). If, 3 more preferably 5 to 65 wt%, and more preferably 40 to 60 wt%.

糖化の終了後、原料と麦芽の混合液は濾過処理がなされ、粗糖化液を得る。なお、必要に応じて60〜70℃の温水(スパージ水)を濾過後の残渣(図示せず)に散布して麦汁(残余の糖化液)を得て、これを前記粗糖化液に混合することもできる。   After completion of saccharification, the mixed solution of raw material and malt is filtered to obtain a crude saccharified solution. In addition, 60-70 degreeC warm water (sparge water) is sprayed on the residue (not shown) after filtration as needed, wort (residual saccharified liquid) is obtained, and this is mixed with the said crude saccharified liquid You can also

得られた粗糖化液はそのまま発酵させることもできるが、ホップを添加し、苦味と香味を付与することもできる。苦味付けのホップを添加する場合は、その添加後、60〜100分間煮沸される。これにより、糖化液中にホップの成分が抽出されると共に、糖化液中の過剰なタンパク質(酵素を含む)を沈殿させて醸造酒を清澄なものにすることができる。なお、ホップとしては、醸造酒に主に苦味を付与するビターホップと主に香りを付与するアロマホップがあるが、これらは単独でも、2種を混合して用いることもできる。 The obtained crude saccharified solution can be fermented as it is, but hops can be added to impart bitterness and flavor. When adding a bitter hop, it is boiled for 60 to 100 minutes after the addition. Thus, the components of the hops are extracted into sugar solution, the excess protein to precipitate (including enzymes) Brewing Zoshu in the saccharified solution may be those fining. As the hop, there are aroma hop to impart predominantly aroma and bitter hop to impart predominantly bitter Brewing Zoshu, it alone can be used in combination of two or.

煮沸により、ホップ粕や凝固したタンパク質が副生されるため、これらは濾過等により除去される。これにより、ホップの成分が抽出された糖化液が得られる。この糖化液は10〜20℃に冷却され、発酵タンクへ送られる。   Since hop koji and coagulated protein are by-produced by boiling, these are removed by filtration or the like. Thereby, the saccharified liquid from which the hop component was extracted is obtained. This saccharified solution is cooled to 10 to 20 ° C. and sent to the fermentation tank.

次に、糖化液は、酵母が添加されてアルコール発酵が行われる。以後、本工程以降の糖化液を「発酵液」という。   Next, yeast is added to the saccharified solution to perform alcoholic fermentation. Hereinafter, the saccharified liquid after this step is referred to as “fermented liquid”.

酵母は、アルコール発酵を行うことができる酵母であれば特に制限はないが、ビール醸造用において一般的に用いられる上面発酵酵母又は下面発酵酵母を用いることができる。上面発酵酵母としては、例えば、サッカロマイセス
セルビシエ(Saccharomyces
cerevisiae)等を挙げることができ、下面発酵酵母としては、例えば、サッカロマイセス
カールスバージェンシス(Saccharomyces
carlsbergensis)等を挙げることができる。
The yeast is not particularly limited as long as it is a yeast capable of performing alcoholic fermentation, but upper fermentation yeast or lower fermentation yeast generally used for brewing beer can be used. Examples of the top fermentation yeast include Saccharomyces (Saccharomyces).
cerevisiae) and the like, and as the bottom fermentation yeast, for example, Saccharomyces (Saccharomyces)
carlsbergensis).

発酵は、主としてエタノールの生産を行う一次発酵工程と、主として該一次発酵工程の後の発酵液の熟成を行う二次発酵工程とからなることが好ましい。   It is preferable that fermentation mainly comprises a primary fermentation process in which ethanol is produced and a secondary fermentation process in which a fermentation liquid is ripened mainly after the primary fermentation process.

一次発酵では、例えば、5〜10℃で8〜12日間発酵が行われる。これにより発酵液中の糖分を酵母が資化してエタノールの生産を行うほか、炭酸ガスの生成や香気成分の生成等が行われる。   In primary fermentation, for example, fermentation is performed at 5 to 10 ° C. for 8 to 12 days. As a result, the sugar in the fermentation broth is assimilated by the yeast to produce ethanol, as well as producing carbon dioxide and aroma components.

二次発酵では、例えば、0〜2℃で20〜40日間発酵が行われる。これにより、一次発酵の後の発酵液の熟成が行われるほか、残存エキスの発酵、一次発酵により発生した炭酸ガスの発酵液中への溶存、発酵液の若臭物質の排出、残存酵母及び混濁物質等の沈殿物の沈下等が行われる。   In the secondary fermentation, for example, fermentation is performed at 0 to 2 ° C. for 20 to 40 days. As a result, the fermentation broth after the primary fermentation is matured, the remaining extract is fermented, the carbon dioxide gas generated by the primary fermentation is dissolved in the fermentation broth, the discharge of young odorous substances from the fermentation broth, residual yeast and turbidity. Subsidence of sediments such as substances is performed.

このようにして得られた醸造酒は、リン酸化オリゴ糖の濃度が200ppm以上のビール又は発泡酒となる。   The brewed liquor thus obtained is a beer or a sparkling liquor having a phosphorylated oligosaccharide concentration of 200 ppm or more.

リン濃度が1125ppmである馬鈴薯澱粉70kg、麦芽105kg、水1.3klであるビールを以下の要領で製造した。   A beer with 70 kg of potato starch having a phosphorus concentration of 1125 ppm, 105 kg of malt and 1.3 kl of water was produced as follows.

(1)糖化
煮沸釜に用意した50℃の湯300Lに馬鈴薯澱粉70kgと麦芽20kgを溶かした後に加熱し、70℃に15分、100℃に10分間保持することにより生澱粉を糊化(α化)した。そして、煮沸釜に水450Lと麦芽85kgを加えて52℃で15分タンパク質分解を行った後、引き続き64℃で40分糖化し、さらに72℃で30分糖化を行うことにより、麦芽および馬鈴薯澱粉由来の糖質を含有する麦汁を得た。
(1) Saccharification After dissolving 70 kg of potato starch and 20 kg of malt in 300 L of 50 ° C. hot water prepared in a boiling kettle, the raw starch is gelatinized by maintaining it at 70 ° C. for 15 minutes and at 100 ° C. for 10 minutes (α ). Then, 450 L of water and 85 kg of malt were added to the boiling kettle and proteolysis was carried out at 52 ° C. for 15 minutes, followed by saccharification at 64 ° C. for 40 minutes and further saccharification at 72 ° C. for 30 minutes, whereby malt and potato starch The wort containing the derived saccharide was obtained.

(2)濾過
糖化終了後、上記(1)で得られた麦汁をろ過槽に移し濾過することにより、1番麦汁を得た。1番麦汁を得た後、この1番麦汁の残渣にスパージ水(70〜80℃)を撒水して2番麦汁を得た。更にこの2番麦汁の残渣にスパージ水(70〜80℃)を撒水して3番麦汁を得た。そして、1番麦汁と2番麦汁と3番麦汁を混合することにより、粗糖化液を得た。
(2) Filtration After completion of saccharification, the wort obtained in (1) above was transferred to a filtration tank and filtered to obtain No. 1 wort. After obtaining No. 1 wort, sparge water (70-80 ° C.) was poured into the residue of No. 1 wort to obtain No. 2 wort. Furthermore, sparged water (70-80 degreeC) was flooded to the residue of this 2nd wort, and 3rd wort was obtained. And the crude saccharified liquid was obtained by mixing 1st wort, 2nd wort, and 3rd wort.

(3)煮沸
(2)で得られた粗糖化液を煮沸釜で加熱し、90分間煮沸した。沸騰すると同時にビターホップとしてテトナング610gを加え、アロマホップとして煮沸開始60分後にカスケード320g、煮沸終了5分前にカスケード160g、煮沸終了と同時にカスケード100gを加え、煮沸を終了した。
(3) Boiling The crude saccharified solution obtained in (2) was heated in a boiling kettle and boiled for 90 minutes. At the same time as boiling, 610 g of Tetonang was added as a bitter hop. Cascade 320 g was added 60 minutes after the start of boiling as aroma hop, 160 g of cascade was added 5 minutes before the end of boiling, and 100 g of cascade was added simultaneously with the end of boiling.

(4)沈殿除去
(3)の煮沸処理で副生したタンパク質の凝固物やホップの粕を除去するために、ワールプールに粗糖化液を移した。そして、タンパク質の凝固物やホップの粕を除去することにより糖化液を清澄化し、発酵用の糖化液を得た。
(4) Precipitation removal The crude saccharified solution was transferred to a whirlpool in order to remove protein coagulum and hop koji produced as a by-product in the boiling treatment of (3). And the saccharified liquid was clarified by removing the coagulum of protein and the cocoon of a hop, and the saccharified liquid for fermentation was obtained.

(5)一次発酵
酵母は秋田今野商店社製の培養酵母ピルスナー(ミュンヘン工科大学、ヴァイエンシュテファンNo.34)109/mlレベル×20Lを使用した。
(5) Primary fermentation As yeast, cultured yeast Pilsner (Munich Institute of Technology, Weihenstephan No. 34) manufactured by Akita Imano Shoten Co., Ltd. 10 9 / ml level × 20 L was used.

発酵用の糖化液を冷却した後、発酵タンクに移し、上記酒母を糖化液に添加し、5〜10℃にて10日間、一次発酵を行った。   After cooling the saccharified liquid for fermentation, it moved to the fermentation tank, the said liquor was added to the saccharified liquid, and primary fermentation was performed at 5-10 degreeC for 10 days.

(6)二次発酵
一次発酵が終了した発酵液を貯酒タンクに移し、最終的に発酵液の温度が1℃になるように温度を調整し、30日間、二次発酵を行った。二次発酵の終了後、瓶詰めを行い、所望のビール(高POビール)を得た。なお、得られたビールのリン酸化オリゴ糖(PO)濃度を測定したところ、600ppmであった。
(6) Secondary fermentation The fermented liquor after the primary fermentation was transferred to a liquor storage tank, the temperature was adjusted so that the temperature of the fermented liquor was finally 1 ° C, and secondary fermentation was performed for 30 days. After the completion of the secondary fermentation, bottling was performed to obtain a desired beer (high PO beer). In addition, when the phosphorylated oligosaccharide (PO) density | concentration of the obtained beer was measured, it was 600 ppm.

リン酸化オリゴ糖(PO)の分析は、Carbo
Pac PA−100カラムを用いたDionex DX−300システムによるHPAEC分析により行った(Kamasaka, H, Uchida, M., Kusaka, K., Yamamoto, K., Yoshikawa, K.,
Okada, S., and Ichikawa, T. (1995) Biosci. Biotechnol. Biochem. 59, 1412-1416)。PO標準品は、ポスカム歯科用クリアドライより精製し、秤量、再溶解したものを標準溶液とした。サンプルについては醸造酒の原液に1:3の割合でエタノールを加え4℃一晩放置後、沈殿物を回収、再溶解したものをサンプル溶液として用い、PO標準溶液とサンプルのPO−2相当ピークを基に定量を行った。
Analysis of phosphorylated oligosaccharides (PO)
The analysis was performed by HPAEC analysis using a Dionex DX-300 system using a Pac PA-100 column (Kamasaka, H, Uchida, M., Kusaka, K., Yamamoto, K., Yoshikawa, K.,
Okada, S., and Ichikawa, T. (1995) Biosci. Biotechnol. Biochem. 59, 1412-1416). The PO standard product was purified from Postum Dental Clear Dry, weighed, and re-dissolved to obtain a standard solution. For the sample, add ethanol to the brewed liquor at a ratio of 1: 3 and leave it overnight at 4 ° C. Then, collect the precipitate and redissolve it as a sample solution. Quantification was performed based on this.

リン濃度が1125ppmである馬鈴薯澱粉に替えて、リン濃度が644ppmである馬鈴薯澱粉を用いたこと以外は、実施例1と同様の要領でビール(低POビール)を製造した。なお、得られたビールのリン酸化オリゴ糖(PO)濃度を測定したところ、218ppmであった。   Beer (low PO beer) was produced in the same manner as in Example 1 except that potato starch having a phosphorus concentration of 644 ppm was used instead of potato starch having a phosphorus concentration of 1125 ppm. In addition, when the phosphorylated oligosaccharide (PO) density | concentration of the obtained beer was measured, it was 218 ppm.

[比較例1]
リン濃度が1125ppmである馬鈴薯澱粉に替えて、リン濃度が226ppmである甘藷澱粉を用いたこと以外は、実施例1と同様の要領でビール(甘藷ビール)を製造した。なお、得られたビールのリン酸化オリゴ糖(PO)濃度を測定したところ、極めて低い濃度(トレース)であった。
[Comparative Example 1]
Beer (sweet potato beer) was produced in the same manner as in Example 1 except that sweet potato starch having a phosphorus concentration of 226 ppm was used instead of potato starch having a phosphorus concentration of 1125 ppm. In addition, when the phosphorylated oligosaccharide (PO) density | concentration of the obtained beer was measured, it was very low density | concentration (trace).

[比較例2]
リン濃度が1125ppmである馬鈴薯澱粉に替えて、リン濃度が140ppmであるコーンスターチを用いたこと以外は、実施例1と同様の要領でビール(コーンビール)を製造した。なお、得られたビールのリン酸化オリゴ糖(PO)濃度を測定したが、極めて低濃度のため検出不能(N.D.)であった。
[Comparative Example 2]
Beer (corn beer) was produced in the same manner as in Example 1 except that corn starch having a phosphorus concentration of 140 ppm was used instead of potato starch having a phosphorus concentration of 1125 ppm. In addition, although the phosphorylated oligosaccharide (PO) density | concentration of the obtained beer was measured, since it was very low concentration, it was undetectable (ND).

[比較例3]
澱粉を用いず、麦芽100%としたこと以外は、実施例1と同様の要領でビール(ラガービール)を製造した。なお、得られたビールのリン酸化オリゴ糖(PO)濃度を測定したが、極めて低濃度のため検出不能(N.D.)であった。
[Comparative Example 3]
Beer (lager beer) was produced in the same manner as in Example 1 except that starch was not used and the malt was 100%. In addition, although the phosphorylated oligosaccharide (PO) density | concentration of the obtained beer was measured, since it was very low concentration, it was undetectable (ND).

Claims (2)

リンの濃度が600ppm以上であり、平均粒径が30μm以下である馬鈴薯澱粉を原料として用い、該馬鈴薯澱粉を麦芽及び水に添加して糖化することにより糖化液を製造する糖化工程と、
該糖化液に酵母を添加してアルコール発酵を行う発酵工程と、
を備えるビール、発泡酒又はビール様アルコール飲料の製造方法。
The concentration of phosphorus Ri der than 600 ppm, a saccharification step for producing a sugar solution by an average particle size using the Der Ru potato starch below 30μm as a raw material, for saccharification the potato starch was added to malt and water,
A fermentation process in which yeast is added to the saccharified solution to perform alcoholic fermentation;
A method for producing beer, sparkling liquor or beer-like alcoholic beverages .
前記馬鈴薯が、とうや、ホッカイコガネ、ワセシロ、エニワ、キタアカリ、さやか、アーリースターチ、男爵薯、コナフブキ、トヨシロ、インカパープル、インカレッド、インカのめざめ、ノーザンルビー、シャドークイーン及びキタムラサキからなる群から選択された1種以上である、請求項1に記載のビール、発泡酒又はビール様アルコール飲料の製造方法。The potato is finally selected from the group consisting of scallops, rosettes, eniwa, kitaakali, sayaka, early starch, baron samurai, konafuki, toyoshiro, inca purple, inca red, inca shark, northern ruby, shadow queen and kitamurasaki The method for producing beer, sparkling liquor or beer-like alcoholic beverage according to claim 1, wherein the beer is one or more.
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