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JPH0328185B2 - - Google Patents
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JPH0328185B2 - - Google Patents

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Publication number
JPH0328185B2
JPH0328185B2 JP58137962A JP13796283A JPH0328185B2 JP H0328185 B2 JPH0328185 B2 JP H0328185B2 JP 58137962 A JP58137962 A JP 58137962A JP 13796283 A JP13796283 A JP 13796283A JP H0328185 B2 JPH0328185 B2 JP H0328185B2
Authority
JP
Japan
Prior art keywords
fermentation
fermented
lactic acid
fermented beverage
germinated
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.)
Expired - Lifetime
Application number
JP58137962A
Other languages
Japanese (ja)
Other versions
JPS6030668A (en
Inventor
Tetsuya Yokota
Hideki Sakamoto
Toshibumi Arimura
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kagome Co Ltd
Original Assignee
Kagome Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kagome Co Ltd filed Critical Kagome Co Ltd
Priority to JP58137962A priority Critical patent/JPS6030668A/en
Publication of JPS6030668A publication Critical patent/JPS6030668A/en
Publication of JPH0328185B2 publication Critical patent/JPH0328185B2/ja
Granted legal-status Critical Current

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  • Non-Alcoholic Beverages (AREA)

Description

【発明の詳細な説明】 本発明は、発酵飲料及びその製造方法、更に詳
しくは発芽麦汁及びホエー中にそれぞれ含まれる
各種の蛋白質、ミネラル、ビタミン等と該ホエー
の蛋白分解処理によつて富化した各種のアミノ
酸、ペプタイド等とを活用し、これらの特定酵母
を用いたアルコール発酵及び食品用の一般乳酸菌
を用いた乳酸発酵の同時発酵による二次的香味を
複合化して飲用に優れた香味を有する、発芽麦汁
とホエーの蛋白分解酵素処理物との混合系の発酵
飲料及びその製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fermented beverage and a method for producing the same, and more specifically, to enriching various proteins, minerals, vitamins, etc. contained in germinated wort and whey by proteolytic treatment of the whey. Utilizing various amino acids, peptides, etc., and combining the secondary flavors through simultaneous fermentation of alcoholic fermentation using these specific yeasts and lactic acid fermentation using general food-grade lactic acid bacteria, we have created an excellent flavor for drinking. The present invention relates to a fermented beverage containing a mixture of germinated wort and whey treated with a proteolytic enzyme, and a method for producing the same.

殻類処理物又は乳製品を主原料として、これら
をアルコール発酵及び乳酸発酵した発酵飲料が各
種提案されている。
Various fermented beverages have been proposed that are made by using processed shellfish products or dairy products as main ingredients and subjecting them to alcoholic fermentation and lactic acid fermentation.

例えば、乳酸発酵乳を高浸透圧下でアルコール
発酵した発酵乳飲料(特公昭50−22102号)、乳酸
発酵乳へ高濃度に酵母を加えてアルコール発酵し
た炭酸含有の発酵乳(特公昭54−17812号)等が
ある。しかし、これらの従来手段は、乳酸発酵と
アルコール発酵とを別々に行なうため、発酵が二
工程にまたがり、得られる発酵液もその香味に深
さやこくが欠ける。
For example, fermented milk drinks made by alcohol fermentation of lactic acid-fermented milk under high osmotic pressure (Special Publication No. 50-22102), carbonic acid-containing fermented milk made by alcohol-fermenting lactic acid-fermented milk by adding yeast at a high concentration (Special Publication No. 17812-1977) No.) etc. However, in these conventional methods, lactic acid fermentation and alcohol fermentation are performed separately, so the fermentation involves two steps, and the resulting fermented liquid lacks depth and richness in flavor.

対して、乳に乳酸菌及び酵母を共生させた発酵
乳製品(特公昭49−11432号)、蛋白分解酵素処理
をした豆乳処理物に乳酸菌及び酵母を共生させた
豆乳酸飲料(特公昭51−36340号)、蒸煮米処理物
を添加した豆乳に乳酸菌及び酵母を共生させた乳
酸飲料(特公昭54−32078号)等がある。これら
は、乳酸発酵とアルコール発酵とを同時に行なう
ため、発酵が一工程で済み、得られる発酵液も前
掲な従来手段に比べればその香味に深さやこくが
ある。ところが、この種の共生による従来手段
は、発酵対象原料も大きな問題であるが、食品用
の一般乳酸菌とサツカロマイセス属の如き食品用
に汎用される一般酵母とを共生させて乳酸発酵と
アルコール発酵とを同時に行なうため、飲用に優
れた発酵飲料を得るに対しての乳酸発酵とアルコ
ール発酵との相互調整が困難であり、得られる発
酵液もこれを直接乃至そのまま希釈して飲用する
には香味それ自体及び特にそのバランスが欠け
る。
On the other hand, fermented milk products in which lactic acid bacteria and yeast coexist in milk (Special Publication No. 11432, 1973), and soy-lactic acid beverages in which lactic acid bacteria and yeast coexist in processed soymilk treated with proteolytic enzymes (Special Publication No. 51-36340). There are also lactic acid drinks (Special Publication No. 32078, 1983), which are made by coexisting lactic acid bacteria and yeast in soybean milk to which processed steamed rice has been added. These methods perform lactic acid fermentation and alcohol fermentation simultaneously, so fermentation only takes one step, and the resulting fermented liquid has a deeper and richer flavor than the above-mentioned conventional methods. However, with conventional means based on this kind of symbiosis, the raw material to be fermented is also a big problem, but it is possible to achieve lactic acid fermentation and alcohol fermentation by coexisting common food-grade lactic acid bacteria and common food-grade yeast such as Satucharomyces. Because both are carried out at the same time, it is difficult to mutually adjust lactic acid fermentation and alcoholic fermentation in order to obtain a fermented beverage that is excellent for drinking. itself and especially its lack of balance.

本発明者らは、叙上の従来欠点を解消しつつ、
原料特性を活用した低アルコール含量の新規発酵
飲料を得るべく鋭意研究した結果、発芽麦汁とホ
エーの蛋白分解酵素処理物との混合系に特定の酵
母と食品用の一般乳酸菌とを共生させて発酵する
ことにより、そして特に発芽麦汁として麦芽エキ
スを用いる場合において、乳酸発酵とアルコール
発酵とが好適に調整され、飲用に優れた複合的香
味を有する発酵飲料の得られることを見出し、本
発明を完成するに至つた。
The present inventors solved the above-mentioned conventional drawbacks, and
As a result of intensive research to obtain a new fermented beverage with low alcohol content that utilizes the characteristics of raw materials, we have developed a system in which a specific yeast and general food-grade lactic acid bacteria coexist in a mixed system of germinated wort and whey treated with proteolytic enzymes. It has been discovered that by fermentation, and especially when malt extract is used as germinated wort, lactic acid fermentation and alcohol fermentation can be suitably adjusted, and a fermented beverage having a complex flavor that is excellent for drinking can be obtained, and the present invention has been made based on the present invention. I was able to complete it.

すなわち本発明は、発芽麦汁とホエーの蛋白分
解酵素処理物との混合系にクレベロマイセス・ラ
クチス(Kluyveromyces lactis)及び/又はク
レベロマイセス・フラギリス(Kluyveromyces
fragilis)と食品用の一般乳酸菌とを共生させて
アルコール発酵と乳酸発酵とを同時に行なうこと
を骨子とする発酵飲料及びその製造方法に係る。
That is, the present invention provides a method for adding Kluyveromyces lactis and/or Kluyveromyces fragilis to a mixed system of germinated wort and whey treated with a proteolytic enzyme.
The present invention relates to a fermented beverage and a method for producing the same, in which alcoholic fermentation and lactic acid fermentation are carried out at the same time by symbiotically coexisting L. fragilis) with food-grade general lactic acid bacteria.

本発明において、発芽麦汁は、大麦、小麦、ひ
え麦、ライ麦、エン麦等の麦類の単品又は混合品
に適当な水分と温度を与え、これらの胚乳中に含
まれる栄養成分を利用して発芽させたものから得
られる汁質である。かかる発芽麦汁として、既に
市販されているような麦芽エキスを用いると、量
産加工現場における入手や保管等の取扱い容易性
に加え、本発明の目的がより良く達成される。通
常、ビールの製造に用いられる麦芽は、幼芽が粒
の2/3〜3/4程度発芽した短麦芽といわれる
ものであるが、本発明において好適例である麦芽
エキスの原料は、幼芽が粒の1.5〜2.0倍程度発芽
した、酸素力が最も強くなつている状態の長麦芽
といわれるもので、これを乾燥して苦味のある根
部を除去し、更に荒砕きしたものを温水でゆつく
り抽出し、得られる抽出液を例えばフイルター濃
縮のような有効成分の分解のない濃縮法で濃縮し
たものが麦芽エキスである。この麦芽エキスは、
ミネラルやビタミン等に富む。
In the present invention, germinated wort is produced by applying appropriate moisture and temperature to barley, wheat, wheat, rye, oats, etc. alone or as a mixture, and utilizing the nutritional components contained in the endosperm of these products. It is a juice obtained from sprouted seeds. If a malt extract that is already commercially available is used as such germinated wort, the objects of the present invention can be better achieved in addition to ease of handling such as acquisition and storage in mass production processing sites. Normally, the malt used in the production of beer is called short malt, in which young germs have germinated at about 2/3 to 3/4 of the grains. This is called long malt, which has germinated to about 1.5 to 2.0 times the grain size and has the strongest oxygen power.It is dried, the bitter roots are removed, and it is further crushed and boiled in warm water. Malt extract is produced and extracted, and the resulting extract is concentrated using a concentration method that does not decompose the active ingredients, such as filter concentration. This malt extract is
Rich in minerals and vitamins.

また本発明において、ホエーはチーズ等の製造
工程で得られる脂肪の少ない一般的な残留副産物
である。このホエーは、ラクトアルブミンやラク
トブログリンのごとき可溶性蛋白質、ミネラル、
ビタミンB2のごとき水溶性ビタミンに富む。既
に各種性状のホエーが市販されており、本発明で
はそれらのいずれを使用してもよいが、粉末状ホ
エーが便利である。そして、かかるホエー又はホ
エーの加水溶液を蛋白分解酵素処理する。具体的
には例えば、粉末状ホエーの略15%(W/V)水
溶液にプロテアーゼ(天野製薬社製のプロテアー
ゼアマノA、同プロテアーゼアマノP、同プロレ
ザー等)を0.1〜0.2%(W/V)加え、37〜40℃
×4時間程度酵素処理する。このように酵素処理
することによつて、ホエー中の蛋白質がアミノ酸
やペプタイドに分解され、後述する混合系の発酵
それ自体及び該発酵によつて得られる発酵液の香
味に好影響を及ぼす。実際、ホエーと該ホエーの
蛋白分解処理物とをアミノ酸分析すると、酵素処
理によつて特に、リジン、アンセリン、フエニル
アラニン、スレオニン及びバリンの生成している
ことが判る。通常、これらホエーの蛋白分解酵素
処理物は、過や遠心分離等で不溶分を除去して
用いる。
Further, in the present invention, whey is a common residual by-product with low fat obtained in the manufacturing process of cheese and the like. This whey contains soluble proteins such as lactalbumin and lactobrobulin, minerals,
Rich in water-soluble vitamins such as vitamin B2 . Whey of various properties is already commercially available, and any of them may be used in the present invention, but powdered whey is convenient. Then, such whey or a hydrolyzed solution of whey is treated with a proteolytic enzyme. Specifically, for example, 0.1 to 0.2% (W/V) of protease (Protease Amano A, Protease Amano P, Proleather, etc. manufactured by Amano Pharmaceutical Co., Ltd.) is added to an approximately 15% (W/V) aqueous solution of powdered whey. ) and 37-40℃
×Enzyme treatment for about 4 hours. By enzymatically treating the whey in this way, the proteins in the whey are decomposed into amino acids and peptides, which has a positive effect on the mixed system fermentation itself and the flavor of the fermented liquid obtained by the fermentation, which will be described later. In fact, amino acid analysis of whey and proteolytic products of whey reveals that lysine, anserine, phenylalanine, threonine, and valine are produced by the enzyme treatment. Usually, these proteolytic enzyme-treated whey products are used after removing insoluble matter by filtration or centrifugation.

本発明では、以上説明したような発芽麦汁とホ
エーの蛋白分解酵素処理物との混合系を所謂共生
発酵する。ホエーの蛋白分解酵素処理物は、共生
発酵に必要な栄養物質的なものとして利用し、ま
た得られる発酵液へ飲用に優れた旨味、こく、ま
ろやかさ等を付与する副材として利用する。そし
てこの際更に、発芽麦汁及びホエーの蛋白分解酵
素処理物に野菜及び/又は果実処理物を加えた混
合系を共生発酵すると、一層優れた複合的香味の
発酵液が得られるのである。野菜はトマト、ニン
ジン等、また果実はリンゴ、ブドウ等、ともに所
望する全てのものが対象になり、これらは、洗
浄・選別した後、必要に応じて適宜剥皮・除芯
し、例えばパルパーやフイニツシヤー等で網過
した搾汁液を使用すればよく、網過の前後に加
熱処理をしてもよい。
In the present invention, a mixed system of germinated wort and whey treated with a proteolytic enzyme as described above is subjected to so-called symbiotic fermentation. Whey treated with proteolytic enzymes is used as a nutritional substance necessary for symbiotic fermentation, and is also used as an adjunct that imparts drinkable flavor, richness, and mellowness to the resulting fermented liquid. At this time, if a mixed system of germinated wort and whey treated with proteolytic enzymes and vegetable and/or fruit treatments is further co-fermented, a fermented liquid with an even more excellent complex flavor can be obtained. Vegetables include tomatoes, carrots, etc., and fruits include apples, grapes, and any other desired items. After washing and sorting, these are peeled and cored as necessary, and then processed using a pulper or finisher. It is sufficient to use the squeezed liquid that has been filtered through a sieve, and heat treatment may be performed before and after the sieve.

本発明の共生発酵において、アルコール発酵に
使用する酵母は、クレベロマイセス・ラクチス及
び/又はクレベロマイセス・フラギリスである。
前掲した従来手段のように、サツカロマイセス・
カールスベルゲンシス(Saccharomyces
carlsbergensis)、サツカロマイセス・セレビジ
エ(Saccharomyces cereviseae)等の食品用に
汎用されている一般酵母を使用すると、同時に進
行する乳酸発酵との発酵バランスが悪く、得られ
る発酵液の香味が劣る。一方、本発明の共生発酵
において、乳酸発酵に使用する乳酸菌は、ラクト
バシルス・ブルガリカス(Lactobacillus
bulugaricus)、ストレプトコツカス・サーモフイ
ラス(Streptococcus thermophilus)、ビフイド
バクテリウム・ロングム(Bifidobacterium
longum)等の食品用の一般乳酸菌である。これ
らは2種以上の乳酸菌を共生させることによつて
一層好ましい共生発酵をすることもできる。
In the symbiotic fermentation of the present invention, the yeast used for alcoholic fermentation is Klevomyces lactis and/or Klevomyces fragilis.
As with the conventional methods mentioned above, Satucharomyces
Carlsbergensis (Saccharomyces)
If general yeasts commonly used for food such as Saccharomyces cerevisiae (carlsbergensis) or Saccharomyces cerevisiae are used, the fermentation balance with the lactic acid fermentation that is occurring at the same time is poor, and the flavor of the resulting fermented liquid is inferior. On the other hand, in the symbiotic fermentation of the present invention, the lactic acid bacteria used for lactic acid fermentation are Lactobacillus bulgaricus.
bulugaricus), Streptococcus thermophilus, Bifidobacterium longum
It is a general food-use lactic acid bacterium such as L. longum). These can also perform more preferable symbiotic fermentation by allowing two or more types of lactic acid bacteria to coexist.

前述した混合系を対象に、クレベロマイセス・
ラクチス及び/又はクレベロマイセス・フラギリ
スを使用したアルコール発酵と、食品用の一般乳
酸菌を使用した乳酸発酵とを同時に進行させる
と、エチルアルコールの生成が比較的遅く、香味
との関連においてアルコール発酵と乳酸発酵との
調整がなされ、特にエチルアルコール含量1%未
満の共生発酵段階においてはそのまま飲用に供し
得る極めて優れた複合的香味の発酵飲料が得られ
る。そしてこの際、発芽麦汁として麦芽エキスを
使用するのが好適であり、共生発酵対象の混合系
中において、麦芽エキス/ホエーの蛋白分解酵素
処理物(固形物換算)=5/1〜40/1(重量比)
にすると、得られる発酵液の香味が特によい。ま
た同様の混合系中において、麦芽エキスの濃度を
5〜50%(W/V)にすると便利である。この場
合、麦芽エキスを高濃度で含有させても共生発酵
に悪影響はなく、しかも得られる発酵液もそれだ
け高濃度になるため、発酵液の保存等取扱い、他
製品への展開利用が容易になる。
Targeting the mixed system mentioned above, Kleveromyces
When alcoholic fermentation using C. lactis and/or Cleveromyces fragilis and lactic acid fermentation using general food-grade lactic acid bacteria proceed simultaneously, the production of ethyl alcohol is relatively slow, and alcoholic fermentation and lactic acid fermentation are difficult to achieve in relation to flavor. Especially in the symbiotic fermentation stage where the ethyl alcohol content is less than 1%, a fermented beverage with an excellent complex flavor that can be consumed as is is obtained. At this time, it is preferable to use malt extract as the germination wort, and in the mixed system for symbiotic fermentation, malt extract/whey treated with proteolytic enzymes (solid matter equivalent) = 5/1 to 40/ 1 (weight ratio)
When this is done, the resulting fermented liquid has a particularly good flavor. Further, in a similar mixing system, it is convenient to adjust the concentration of malt extract to 5 to 50% (W/V). In this case, even if malt extract is contained at a high concentration, there will be no adverse effect on the symbiotic fermentation, and the resulting fermentation liquid will also have a correspondingly higher concentration, making it easier to store and handle the fermentation liquid, and to use it in other products. .

具体的に共生発酵は、発芽麦汁とホエーの蛋白
分解酵素処理物(更には野菜及び/又は果実処理
物)との混合溶液を、例えば重炭酸カルシウムの
如きアルカリ剤でPH6.3程度に調整し、95℃達温
程度に加熱殺菌した後、冷却したものに、予備培
養した前記の酵母及び別に予備培養した食品用の
一般乳酸菌を加えて行なう。酵母及び乳酸菌の添
加量は、それぞれの性質、活性度、所望する発酵
液の品質等にもよるが、大略、基質1ml当り1×
105〜5×106cellsとする。発酵中は外部からの雑
菌汚染を厳重防止し、発酵温度は20〜50℃の範囲
でよいが、25〜40℃に維持するのが好ましい。発
酵温度が低すぎると、共生発酵に長時間を要し、
逆に発酵温度が高すぎると、得られる発酵液の香
味が悪い。所定の混合系に、前述のごとく酵母及
び乳酸菌を加え、25〜40℃の温度で20〜35時間共
生発酵させ、PH4.0〜5.0、エチルアルコール0.5〜
1.0%(W/V)、乳酸100〜300mg%(W/V、滴
定酸度を乳酸換算したもの、以下同じ)とした発
酵液が最良である。
Specifically, in symbiotic fermentation, a mixed solution of germinated wort and whey treated with proteolytic enzymes (and further processed vegetables and/or fruits) is adjusted to a pH of about 6.3 with an alkaline agent such as calcium bicarbonate. After heating and sterilizing to a temperature of about 95°C, the pre-cultured yeast mentioned above and separately pre-cultured general lactic acid bacteria for food are added to the cooled mixture. The amount of yeast and lactic acid bacteria added depends on their properties, activity, desired quality of fermentation liquid, etc., but approximately 1x per ml of substrate.
10 5 to 5×10 6 cells. During fermentation, bacterial contamination from the outside is strictly prevented, and the fermentation temperature may be in the range of 20 to 50°C, but preferably maintained at 25 to 40°C. If the fermentation temperature is too low, symbiotic fermentation will take a long time,
On the other hand, if the fermentation temperature is too high, the flavor of the fermented liquid obtained will be poor. Yeast and lactic acid bacteria are added to the predetermined mixed system as described above, and symbiotic fermentation is carried out at a temperature of 25 to 40°C for 20 to 35 hours, pH 4.0 to 5.0, and ethyl alcohol 0.5 to
The best fermentation liquid is 1.0% (W/V) and lactic acid 100-300 mg% (W/V, titratable acidity converted into lactic acid, the same applies hereinafter).

第1図は、麦芽エキス(三共フーズ社製、三共
モルトB2)を10%(W/V)含有し、ホエーの
蛋白分解酵素処理物〔粉末状ホエーの15%(W/
V)水溶液にプロテアーゼ(天野製薬社製、プロ
テアーゼアマノP)を0.20%(W/V)加えて37
〜40℃×4時間酵素処理したものの遠心分離液〕
を2%(W/V)含有する混合水溶液を、重炭酸
カルシウムでPH6.3に調整し、これを95℃達温で
加熱殺菌して30冷却した後、予備培養したクレベ
ロマイセス・ラクチスを基質1ml当たり3×
105cells、また別に予備培養したラクトバシル
ス・ブルガリカス及びストレプトコツカス・サー
モフイラスをそれぞれ基質1ml当たり3×
105cellsとなるように加え、30℃で静置発酵した
ときの、共生発酵状況を例示するグラフである。
また第2図は、麦芽エキス(第1図の場合と同じ
もの)を18%(W/V)、ホエーの蛋白分解酵素
処理物(第1図の場合と同じ遠心分離液)1.7%
(W/V)及びトマト処理物(洗浄・選別したト
マトの0.5mmφ孔径過金網を装着したフイニツ
シヤーによる搾汁液)10%(W/V)をそれぞれ
含有する混合水溶液を、以下第1図の場合と同様
に静置発酵したときの、共生発酵状況を例示する
グラフである。
Figure 1 shows a product containing 10% (W/V) of malt extract (Sankyo Malt B 2 manufactured by Sankyo Foods Co., Ltd.) and a proteolytic enzyme-treated whey product [15% (W/V) of powdered whey.
V) Add 0.20% (W/V) of protease (manufactured by Amano Pharmaceutical Co., Ltd., Protease Amano P) to the aqueous solution.
Centrifuged liquid from ~40°C x 4 hours enzyme treatment]
A mixed aqueous solution containing 2% (W/V) of K. lactis was adjusted to pH 6.3 with calcium bicarbonate, heat sterilized at 95°C, cooled for 30 minutes, and precultured Cleveromyces lactis was added to 1 ml of substrate. Win 3x
10 5 cells, separately precultured Lactobacillus bulgaricus and Streptococcus thermophilus each at 3x per ml of substrate.
It is a graph illustrating the symbiotic fermentation situation when 10 5 cells were added and fermented statically at 30°C.
In addition, Figure 2 shows malt extract (same as in Figure 1) at 18% (W/V) and whey proteolytic enzyme-treated product (same centrifuged liquid as in Figure 1) at 1.7%.
A mixed aqueous solution containing 10% (W/V) and 10% (W/V) of tomato processed product (juice extracted from washed and sorted tomatoes by a finisher equipped with a 0.5 mm diameter wire screen) was prepared as shown in Figure 1 below. It is a graph illustrating the symbiotic fermentation situation when static fermentation is carried out similarly to.

第1図と第2図で例示するように、エチルアル
コールの生成は比較的緩慢であり、香味関連にお
いてアルコール発酵と乳酸発酵との発酵バランス
が程よく調整されていて、各図面の範囲内では発
酵時間が25〜30(時)の段階で飲用に好適の発酵
液が得られている〔図中、曲線11,21=乳酸
(mg%、(W/V)、曲線12,22=エチルアル
コール(%、(W/V)、液体クロマトグラフイ
ー)、曲線13,23=PH、曲線14,24=酵
母生菌数(logN/1ml、以下生菌数は同じ)、曲
線15,25=クラトバシルス・ブルガリカス生
菌数、曲線16,26=ストレプトコツカス・サ
ーモフイラス生菌数は、横軸は発酵時間(時)〕。
As illustrated in Figures 1 and 2, the production of ethyl alcohol is relatively slow, and the fermentation balance between alcoholic fermentation and lactic acid fermentation is well adjusted in relation to flavor, and within the range of each figure, ethyl alcohol is produced relatively slowly. A fermented liquid suitable for drinking was obtained at a time of 25 to 30 hours (in the figure, curves 11 and 21 = lactic acid (mg%, (W/V), curves 12 and 22 = ethyl alcohol ( %, (W/V), liquid chromatography), curves 13, 23 = PH, curves 14, 24 = yeast viable count (logN/1ml, hereinafter the viable counts are the same), curves 15, 25 = Clatobacillus. bulgaricus viable count, curve 16, 26 = Streptococcus thermophilus viable count, the horizontal axis is fermentation time (hours)].

かくして得られる発酵液は、ここに含まれる菌
体それ自身も有用であるため、酵母及び乳酸菌を
含有したままで、又はこれらを過や遠心分離で
除去した後に、そのまま製品(例えばチルド製
品、又は殺菌後に通常の瓶や缶詰製品)化するこ
ともでき、更に必要に応じて、該発酵液を濃縮、
乾燥及び/又は調整して製品化する。濃縮は例え
ば逆浸透圧法又は真空法で、また乾燥は例えば噴
霧乾燥法又は凍結乾燥法でよい。これらの製品化
最終段階において、糖類や香料等を加えることも
できる。勿論、発芽麦汁を高濃度で共生発酵した
場合、発酵液を濃縮や乾燥した場合には、製品化
の際に又は飲用の際に適宜希釈する。また、発酵
液をそのまま飲用し得る濃度溶液で製品化する場
合には、カーボネーシヨンすると、さわやかな発
酵飲料が得られる。この場合のカーボネーシヨン
は、製品中の炭酸ガスボリユームが2.0〜2.5程度
となるようにするのがよい。
The fermented liquid thus obtained is useful as a whole, so it can be used as a product (for example, a chilled product, or After sterilization, it can be made into regular bottles or canned products, and if necessary, the fermented liquid can be concentrated or
Dry and/or adjust the product. Concentration may be carried out, for example, by reverse osmosis or vacuum, and drying may be carried out, for example, by spray drying or freeze drying. Sugars, fragrances, etc. can also be added at the final stage of commercialization. Of course, when the germinated wort is co-fermented at a high concentration, or when the fermentation liquid is concentrated or dried, it is diluted as appropriate when producing a product or drinking it. In addition, if the fermented liquid is to be manufactured into a product with a concentrated solution that can be drunk as it is, a refreshing fermented beverage can be obtained by carbonation. In this case, carbonation is preferably such that the carbon dioxide volume in the product is about 2.0 to 2.5.

各製品はいずれも、原料である発芽麦汁及びホ
エー(更には野菜及び/又は果実処理物)中に含
まれる各種の蛋白質、ミネラル、ビタミン等と該
ホエーの蛋白分解酵素処理によつて富化した各種
のアミノ酸、ペプタイド等が活用されており、飲
用に優れた複合的香味を有する。実際、これらの
製品と、他の諸条件を同一にしつつ単に酵母とし
てサツカロマイセス属を用いたことだけが異なる
発酵飲料とを官能評価しても(発芽麦汁やホエー
の蛋白分解酵素処理物を使用しない場合のよう
に、原料内容が欠ける又は異なる場合も同様であ
るが)、1%の危険率で、本発明に係る発酵飲料
について好結果が有意検定されるのである(検査
員20名×3回繰り返し×2点又は3点嗜好順位
法)。
Each product is enriched with various proteins, minerals, vitamins, etc. contained in the raw materials, germinated wort and whey (and processed vegetables and/or fruits), as well as by processing the whey with proteolytic enzymes. Various amino acids, peptides, etc. are utilized, and it has a complex flavor that is excellent for drinking. In fact, a sensory evaluation of these products and a fermented beverage with the same other conditions but differing only in the use of Saccharomyces as the yeast (proteolytic enzyme-treated germinated wort or whey was used) The same applies to cases where the content of raw materials is missing or different, such as when the ingredients are not present), but a positive result for the fermented beverage according to the present invention is significantly tested at a risk rate of 1% (20 inspectors x 3). (times repeated x 2 points or 3 points preference ranking method).

実施例 1 麦芽エキス(前掲のもの)の40%(W/V)水
溶液80容量部と、ホエーの蛋白分解酵素処理物
〔粉末状ホエーの6%(W/V)水溶液にプロテ
アーゼ(天野製薬社製、プロテアーゼアマノA)
を0.15%(W/V)加え、38℃で4時間酵素処理
し、処理液を遠心分離したもの〕20重量部との混
合溶液を、重炭酸カルシウムでPH6.3に調整し、
これを95℃達温で加熱殺菌して35℃に冷却した
後、予備培養したクレベロマイセス・ラクチスと
別に予備培養したラクトバシルス・ブルガリカス
とをそれぞれ基質1ml当たり2×106cellsとなる
ように加え、外部からの菌数汚染を防止しつつ、
35℃で30時間静置発酵した。得られた発酵液のエ
チルアルコール1.2%(W/V)、乳酸420mg%
(W/V)、PH4.1であつた。この発酵液を遠心分
離して発酵母液を得た。
Example 1 80 parts by volume of a 40% (W/V) aqueous solution of malt extract (mentioned above) and protease-treated whey [6% (W/V) aqueous solution of powdered whey were mixed with protease (Amano Pharmaceutical Co., Ltd.)] manufactured by Protease Amano A)
0.15% (W/V) was added, enzyme-treated at 38°C for 4 hours, and the treated solution was centrifuged] A mixed solution of 20 parts by weight was adjusted to pH 6.3 with calcium bicarbonate,
After heating and sterilizing this at a temperature of 95°C and cooling it to 35°C, pre-cultured Cleveromyces lactis and separately pre-cultured Lactobacillus bulgaricus were added at a density of 2 x 10 6 cells per ml of substrate. While preventing bacterial contamination from outside,
Static fermentation was performed at 35°C for 30 hours. Ethyl alcohol 1.2% (W/V), lactic acid 420mg% of the obtained fermentation liquid
(W/V), PH4.1. This fermentation liquid was centrifuged to obtain a fermentation mother liquor.

そして、発酵母液を3倍水希釈し、希釈液99
+砂糖200g+香料(レモン系)0.5gの割合で調
整した後、95℃達温で加熱殺菌して10℃に冷却
し、発酵飲料(実施例)を製造した。
Then, dilute the fermentation mother liquor 3 times with water, and dilute the diluted solution with 99% water.
After adjusting the ratio of + 200 g of sugar + 0.5 g of fragrance (lemon type), the mixture was heat sterilized at a temperature of 95°C and cooled to 10°C to produce a fermented beverage (Example).

他の諸条件を同一にしつつ並行して、酵母にサ
ツカロマイセス・セレビジエを用いたことだけが
異なる発酵飲料(比較例)を製造したが、実施例
と比較例とを官能評価すると、実施例に好効果が
有意検定された(検査員20名×2回繰り返し×2
点嗜好×危険率1%)。
A fermented beverage (comparative example) was produced in parallel with the other conditions being the same, but the only difference was that Saccharomyces cerevisiae was used as the yeast. Sensory evaluation of the example and comparative example showed that the example had a preference. The effect was significantly tested (20 inspectors x 2 repetitions x 2)
point preference x risk rate 1%).

実施例 2 実施例1と同様にして発酵母液を得た。Example 2 Fermentation mother liquor was obtained in the same manner as in Example 1.

そして、発酵母液を3倍水希釈し、希釈液99
+砂糖200g+香料(柑橘系)0.5gの割合で調整
し、そのままチルド(5℃)の発酵飲料(実施
例)を製造した。
Then, dilute the fermentation mother liquor 3 times with water, and dilute the diluted solution with 99% water.
A chilled (5° C.) fermented beverage (Example) was produced by adjusting the ratio of +200g sugar +0.5g flavor (citrus).

官能評価は実施例1の場合と同様であつた。 The sensory evaluation was the same as in Example 1.

実施例 3 実施例1と同様にして発酵母液を得た。Example 3 Fermentation mother liquor was obtained in the same manner as in Example 1.

そして、発酵母液を3倍水希釈し、以下実施例
1と同様に調整、加熱殺菌、冷却(但し5℃)及
び遠心分離した後、炭酸ガスボリユーム2.3を目
標にカーボネーシヨンして発酵飲料(実施例)を
製造した。
Then, the fermentation mother liquor was diluted 3 times with water, and then adjusted, heat sterilized, cooled (5°C), and centrifuged in the same manner as in Example 1, and then carbonated to a carbon dioxide gas volume of 2.3 to obtain a fermented beverage ( Example) was manufactured.

官能評価は実施例1の場合と同様であつた。 The sensory evaluation was the same as in Example 1.

実施例 4 実施例1と同様にして発酵母液を得た。Example 4 Fermentation mother liquor was obtained in the same manner as in Example 1.

そして、発酵母液を減圧下に濃縮し(80℃)、
更に凍結乾燥した。得られた乾燥物30g+砂糖6
g+香料(レモン系)0.001gの割合で調整し、
これを300mlに加水溶解して発酵飲料(実施例)
を製造した。
Then, the fermentation mother liquor was concentrated under reduced pressure (80°C),
It was further freeze-dried. 30 g of dried product + 6 sugar
Adjust the ratio of g + fragrance (lemon type) 0.001 g,
Fermented beverage by dissolving this in 300ml of water (Example)
was manufactured.

官能評価は実施例1の場合と同様であつた。 The sensory evaluation was the same as in Example 1.

実施例 5 麦芽エキス(前掲のもの)の15%(W/V)水
溶液70容量部と、ホエーの蛋白分解酵素処理物
〔粉末状ホエーの2%(W/V)水溶液にプロテ
アーゼ(天野製薬社製、プロテアーゼアマノP)
を0.10%(W/V)加え、以下実施例1と同様に
処理したもの〕20容量部と、トマト処理物〔洗
浄・選別したトマト(品種はカゴメ81)を破砕
し、85℃達温で加熱した後、2mmφ孔径の過網
を装着したパルパーで搾汁し、搾汁液を30℃に冷
却したもの〕10容量部との混合溶液を、重炭酸ナ
トリウムでPH6.3に調整し、これを95℃達温で加
熱殺菌して30℃に冷却した後、それぞれ別々に予
備培養した、クレベレマイセス・ラクチス、クレ
ベロマイセス・フラギリス、ラクトバシルス・ブ
リガリカス、ストレプトコツカス・サーモフイラ
スを各々、基質1ml当たり3×105cellsとなるよ
うに加え、外部からの菌的汚染を防止しつつ、30
℃で27時間静置発酵した。得られた発酵液のエチ
ルアルコール0.9%(W/V)、乳酸260mg%
(W/V)、PH4.1であつた。
Example 5 70 parts by volume of a 15% (W/V) aqueous solution of malt extract (mentioned above) and protease-treated whey [2% (W/V) aqueous solution of powdered whey were mixed with protease (Amano Pharmaceutical Co., Ltd.)] manufactured by Protease Amano P)
Added 0.10% (W/V) and treated in the same manner as in Example 1] 20 volume parts and tomato processed product [washed and sorted tomatoes (variety: Kagome 81) were crushed and heated to 85°C. After heating, the juice was squeezed using a pulper equipped with a mesh with a 2 mmφ hole diameter, and the squeezed liquid was cooled to 30°C. A mixed solution of 10 parts by volume was adjusted to pH 6.3 with sodium bicarbonate. After heating and sterilizing at 95°C and cooling to 30°C, Klebelomyces lactis, Klebelomyces fragilis, Lactobacillus brigaricus, and Streptococcus thermophilus were each precultured separately at 3 x 10 5 per ml of substrate. 30 cells while preventing bacterial contamination from the outside.
Static fermentation was carried out at ℃ for 27 hours. Ethyl alcohol 0.9% (W/V), lactic acid 260mg% of the obtained fermentation liquid
(W/V), PH4.1.

そして、この発酵液の遠心分離液99+砂糖
200g+香料(レモン系)0.5gの割合で調整した
後、95℃達温で加熱殺菌して10℃に冷却し、発酵
飲料(実施例)を製造した。
And centrifuged liquid of this fermentation liquid 99 + sugar
After adjusting the ratio of 200g + 0.5g of fragrance (lemon type), it was heat sterilized at 95°C and cooled to 10°C to produce a fermented beverage (Example).

官能評価は実施例1の場合と同様であつた。 The sensory evaluation was the same as in Example 1.

【図面の簡単な説明】[Brief explanation of drawings]

第1図と第2図は本発明における共生発酵状況
を各別に例示するグラフである。 11,21……乳酸曲線、12,22……エチ
ルアルコール曲線、13,23……PH曲線、1
4,24……酵母生菌数曲線、15,25……ラ
クトバシルス・ブルガリカス生菌数曲線、16,
26……ストレプトコツカス・サーモフイラス生
菌数曲線。
FIGS. 1 and 2 are graphs illustrating the symbiotic fermentation situation in the present invention. 11,21...Lactic acid curve, 12,22...Ethyl alcohol curve, 13,23...PH curve, 1
4,24...Yeast viable count curve, 15,25...Lactobacillus bulgaricus viable count curve, 16,
26...Streptococcus thermophilus viable count curve.

Claims (1)

【特許請求の範囲】 1 発芽麦汁とホエーの蛋白分解酵素処理物との
混合系のクレベロマイセス・ラクチス及び/又は
クレベロマイセス・フラギリスと食品用の一般乳
酸菌との共生による発酵液、該発酵液の濃縮物又
は該発酵液の乾燥物を主成分とする、エチルアル
コール含有1%(W/V)未満の発酵飲料。 2 発芽麦汁として麦芽エキスを用いる特許請求
の範囲第1項記載の発酵飲料。 3 発芽麦汁とホエーの蛋白分解酵素処理物との
混合系のクレベロマイセス・ラクチス及び/又は
クレベロマイセス・フラギリスと食品用の一般乳
酸菌との共生による発酵液、該発酵液の濃縮物又
は該発酵液の乾燥物を主成分とし、酵母及び乳酸
菌を含有する、エチルアルコール含量1%(W/
V)未満の発酵飲料。 4 発芽麦汁として麦芽エキスを用いる特許請求
の範囲第3項記載の発酵飲料。 5 発芽麦汁とホエーの蛋白分解酵素処理物と野
菜及び/又は果実処理物との混合系のクレベロマ
イセス・ラクチス及び/又はクレベロマイセス・
フラギリスと食品用の一般乳酸菌との共生による
発酵液、該発酵液の濃縮物又は該発酵液の乾燥物
を主成分とする、エチルアルコール含量1%
(W/V)未満の発酵飲料。 6 発芽麦汁として麦芽エキスを用いる特許請求
の範囲第5項記載の発酵飲料。 7 発芽麦汁とホエーの蛋白分解酵素処理物との
混合系をPH調整し、殺菌して冷却した後、予備培
養した酵母であるクレベロマイセス・ラクチス及
び/又はクレベロマイセス・フラギリスと、別に
予備培養した食品用の一般乳酸菌とを加えて所謂
アルコール発酵と乳酸発酵とを同時に行ない、エ
チルアルコール含量1%未満の段階で発酵を終了
させ、次いで酵母及び乳酸菌を分離して発酵液を
得、これを必要に応じて濃縮、乾燥及び/又は調
整する発酵飲料の製造方法。 8 発酵したものをカーボネーシヨンする特許請
求の範囲第7項記載の発酵飲料の製造方法。 9 発芽麦汁として麦芽エキスを用いる特許請求
の範囲第7項又は第8項記載の発酵飲料の製造方
法。 10 麦芽エキス/ホエーの蛋白分解酵素処理物
(固形物換算)=5/1〜40/1(重量比)の混合
系を対象とする特許請求の範囲第9項記載の発酵
飲料の製造方法。 11 麦芽エキスの濃度を5〜50%(W/V)で
発酵する特許請求の範囲第9項又は第10項記載
の発酵飲料の製造方法。 12 温度を25〜40℃で発酵する特許請求の範囲
第7項〜第11項のいずれか一つの項記載の発酵
飲料の製造方法。
[Scope of Claims] 1. A fermentation liquid resulting from the symbiosis of Cleveromyces lactis and/or Cleveromyces fragilis in a mixed system of germinated wort and whey treated with proteolytic enzymes and food-grade general lactic acid bacteria, and concentration of the fermentation liquid. A fermented beverage containing less than 1% (W/V) ethyl alcohol, the main component of which is a dried product of the fermented liquor. 2. The fermented beverage according to claim 1, which uses malt extract as the germinated wort. 3. Fermentation liquid produced by the symbiosis of Cleveromyces lactis and/or Cleveromyces fragilis in a mixed system of germinated wort and whey treated with proteolytic enzymes and food-grade general lactic acid bacteria, a concentrate of the fermentation liquid, or a fermentation liquid of the fermentation liquid. Mainly composed of dry matter, containing yeast and lactic acid bacteria, with an ethyl alcohol content of 1% (W/
V) Fermented beverages with less than 4. The fermented beverage according to claim 3, which uses malt extract as the germinated wort. 5 Cleveromyces lactis and/or Cleveromyces lactis mixed with a proteolytic enzyme-treated product of germinated wort and whey and a vegetable and/or fruit treated product
Fermented liquid resulting from the symbiosis of L. fragilis and general food-grade lactic acid bacteria, a concentrate of the fermented liquid, or a dried product of the fermented liquid as the main component, with an ethyl alcohol content of 1%.
(W/V) Fermented beverage. 6. The fermented beverage according to claim 5, which uses malt extract as the germinated wort. 7. A mixed system of germinated wort and whey treated with a proteolytic enzyme is adjusted to pH, sterilized and cooled, and then pre-cultured yeast Kleberomyces lactis and/or Kleberomyces fragilis is added to a food product that is pre-cultured separately. So-called alcohol fermentation and lactic acid fermentation are carried out simultaneously by adding common lactic acid bacteria, and the fermentation is terminated when the ethyl alcohol content is less than 1%.Then, yeast and lactic acid bacteria are separated to obtain a fermentation liquid, which is used as needed. A method for producing a fermented beverage, concentrating, drying and/or adjusting accordingly. 8. The method for producing a fermented beverage according to claim 7, which comprises carbonating the fermented beverage. 9. The method for producing a fermented beverage according to claim 7 or 8, using malt extract as the germinated wort. 10. The method for producing a fermented beverage according to claim 9, which is directed to a mixed system of malt extract/whey treated with a proteolytic enzyme (in terms of solid matter) = 5/1 to 40/1 (weight ratio). 11. The method for producing a fermented beverage according to claim 9 or 10, which comprises fermenting the malt extract at a concentration of 5 to 50% (W/V). 12. The method for producing a fermented beverage according to any one of claims 7 to 11, wherein the fermentation is carried out at a temperature of 25 to 40°C.
JP58137962A 1983-07-28 1983-07-28 Fermented drink and its preparation Granted JPS6030668A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58137962A JPS6030668A (en) 1983-07-28 1983-07-28 Fermented drink and its preparation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58137962A JPS6030668A (en) 1983-07-28 1983-07-28 Fermented drink and its preparation

Publications (2)

Publication Number Publication Date
JPS6030668A JPS6030668A (en) 1985-02-16
JPH0328185B2 true JPH0328185B2 (en) 1991-04-18

Family

ID=15210791

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Country Link
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CN107267343B (en) * 2017-08-22 2020-11-06 鲁东大学 A kind of additive-free mulberry health-care wine and preparation method thereof
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