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JPH04615B2 - - Google Patents
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JPH04615B2 - - Google Patents

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Publication number
JPH04615B2
JPH04615B2 JP58095225A JP9522583A JPH04615B2 JP H04615 B2 JPH04615 B2 JP H04615B2 JP 58095225 A JP58095225 A JP 58095225A JP 9522583 A JP9522583 A JP 9522583A JP H04615 B2 JPH04615 B2 JP H04615B2
Authority
JP
Japan
Prior art keywords
lactic acid
fermentation
whey
malt extract
treated
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
JP58095225A
Other languages
Japanese (ja)
Other versions
JPS59220153A (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 JP9522583A priority Critical patent/JPS59220153A/en
Publication of JPS59220153A publication Critical patent/JPS59220153A/en
Publication of JPH04615B2 publication Critical patent/JPH04615B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は乳酸発酵飲料の製造方法、更に詳しく
は麦芽エキス及びホエーにそれぞれ含まれる各種
のミネラル、ビタミン等をそのまま活用し、これ
らの効率的な乳酸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乳酸発酵飲料の製
造方法に関する。
[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a method for producing a lactic acid fermented beverage, and more specifically, to an efficient method for producing a lactic acid fermented beverage by directly utilizing various minerals, vitamins, etc. contained in malt extract and whey. The present invention relates to a method for producing a lactic acid fermented beverage that has an excellent drinkable flavor by combining secondary flavors caused by lactic acid fermentation.

<従来の技術、その問題点> 麦芽を原料とする発酵飲料の代表例として、こ
れをアルコール発酵したビールやウイスキー等の
アルコール飲料が広く飲用されている。
<Prior art and its problems> Alcoholic beverages such as beer and whiskey produced by alcohol fermentation of malt are widely consumed as typical examples of fermented beverages using malt as a raw material.

一方、麦芽又は穀類胚芽を原料とする発酵飲料
の他の例として、これを乳酸発酵した乳酸発酵飲
料が提案されている(特公昭53−41223号、特公
昭57−37315号)。またホエー等を原料とする乳酸
発酵飲料(特開昭54−129164号)、乳蛋白固形分
の酵素処理物等を原料とする乳酸発酵飲料(特開
昭55−77859号)も提案されている。
On the other hand, as another example of a fermented beverage using malt or grain germ as raw materials, a lactic acid fermented beverage obtained by fermenting malt or grain germ with lactic acid has been proposed (Japanese Patent Publication No. 41223-1983, Japanese Patent Publication No. 37315-1983). In addition, lactic acid fermented drinks made from whey etc. (Japanese Patent Application Laid-open No. 129164/1982) and lactic acid fermented drinks made from enzyme-treated milk protein solids (Japanese Patent Application Laid-open No. 77859/1982) have also been proposed. .

これらの乳酸発酵飲料は、広く飲用されている
アルコール飲料とは異なり、非アルコール飲料で
ある点に特長を有し、麦芽やホエー等に含まれる
種々のミネラル、ビタミン等を利用している点で
も特長を有する。
Unlike widely consumed alcoholic beverages, these lactic acid fermented beverages are unique in that they are non-alcoholic beverages, and they also utilize various minerals, vitamins, etc. contained in malt, whey, etc. It has characteristics.

しかし、かかる従来品には、これを得るに乳酸
発酵が全体として非効率的で、しかも飲用に優れ
た香味を有するとはいい難いという問題点があ
る。
However, such conventional products have the problem that the lactic acid fermentation used to obtain them is generally inefficient, and it is difficult to say that they have an excellent flavor for drinking.

<発明が解決しようとする問題点、その解決手段
> 本発明は叙上の如き従来の問題点を解決する改
良された乳酸発酵飲料の製造方法を提供するもの
である。
<Problems to be Solved by the Invention and Means for Solving the Problems> The present invention provides an improved method for producing lactic acid fermented beverages that solves the conventional problems as described above.

しかして本発明者らは、麦芽やホエーに含まれ
る各種のミネラル、ビタミン等を活用した非アル
コール性の乳酸発酵飲料であつて、乳酸発酵が全
体として効率的に行なわれ、しかも飲用に優れた
香味を有する乳酸発酵飲料を得るべく鋭意研究し
た結果、麦芽エキスとホエーの蛋白分解酵素処理
物との混合溶液であつて該麦芽エキスを所定量含
有する混合溶液を乳酸発酵して発酵母液を得るこ
とが正しく好適であることを見出し、本発明を完
成するに到つた。
Therefore, the present inventors have developed a non-alcoholic lactic acid fermented beverage that utilizes various minerals, vitamins, etc. contained in malt and whey, in which lactic acid fermentation is carried out efficiently as a whole, and which is excellent for drinking. As a result of intensive research to obtain a flavored lactic acid fermented beverage, we obtained a fermentation mother liquor by lactic acid fermentation of a mixed solution of malt extract and a proteolytic enzyme-treated product of whey, which contains a predetermined amount of the malt extract. The inventors have found that this is correct and suitable, and have completed the present invention.

すなわち本発明は、麦芽エキスとホエーの蛋白
分解酵素処理物との混合溶液であつて該麦芽エキ
スを30〜60%(W/V)含有する混合溶液をPH調
整し、殺菌して冷却した後、予備培養した乳酸菌
を加えて乳酸発酵することにより発酵母液を得、
該発酵母液を水希釈して調整することを特徴とす
る乳酸発酵飲料の製造方法に係る。
That is, the present invention is a mixed solution of malt extract and whey treated with a proteolytic enzyme, which contains 30 to 60% (W/V) of the malt extract, after adjusting the pH, sterilizing it, and cooling it. , a fermentation mother liquor is obtained by adding pre-cultured lactic acid bacteria and carrying out lactic acid fermentation,
The present invention relates to a method for producing a lactic acid fermented beverage, which comprises preparing the fermented mother liquor by diluting it with water.

本発明において、麦芽エキスは市販品を用いる
ことができる。該麦芽エキスはアルコール飲料の
製造に用いる麦芽に比べて量産加工現場における
入手や保管等の取扱い容易性に優れる。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、本発明で用い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、酵素力が最も
強くなつている状態の長発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, commercially available malt extracts can be used. The malt extract is easier to handle in terms of acquisition and storage in mass-production processing sites than malt used in the production of alcoholic beverages. Normally, the malt used for beer production has young buds that are about 2/2 of the size of the grains.
It is called short malt that has germinated to the extent of 3 to 3/4, but the raw material for the malt extract used in the present invention is short malt that has germinated to the extent of 1.5 to 2.0 times the germination of the grains and has the strongest enzymatic power. This is called long germination,
This is dried to remove the bitter roots, and then crushed and slowly extracted with warm water, and the resulting extract is concentrated using a concentration method that does not decompose the active ingredients, such as filter concentration. It is malt extract. 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
を用いることができる。このホエーは、乳糖を主
成分とするが、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。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
ずれを用いてもよいが、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、後述する混合溶液の乳酸発酵における発酵
効率や該発酵によつて得られる発酵母液の香味に
著しい好影響を及ぼす。実際、ホエーと該ホエー
の蛋白分解酵素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、濾過や遠心分離等で不溶分を除
去して用いる。
Further, in the present invention, as the whey, a common residual by-product with low fat obtained in the manufacturing process of cheese and the like can be used. This whey is mainly composed of lactose, but also contains soluble proteins such as lactalbumin and lactobrobulin, minerals, and vitamins.
Rich in water-soluble vitamins such as B2 . Whey of various properties is 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 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.
% (W/V) and enzyme treatment at 37-40°C for about 4 hours. By enzymatic treatment in this way,
Proteins in whey are decomposed into amino acids and peptides, which has a significant positive effect on the fermentation efficiency in lactic acid fermentation of a mixed solution, which will be described later, and on the flavor of the fermentation mother liquor obtained by the fermentation. In fact, when we analyze the amino acids of whey and the proteolytic enzyme-treated product of whey, we find that
It can be seen that lysine, anserine, phenylalanine, threonine, and valine are particularly produced by the enzyme treatment. Usually, these proteolytic enzyme-treated whey products are used after removing insoluble matter by filtration, centrifugation, or the like.

本発明では、以上説明したような麦芽エキスと
ホエーの蛋白分解酵素処理物との混合溶液であつ
て該麦芽エキスを30〜60%(W/V)含有する混
合溶液を乳酸発酵する。麦芽エキス単独やホエー
の蛋白分解酵素処理物単独、更には麦芽エキスと
ホエーの蛋白分解酵素処理物との混合溶液であつ
ても麦芽エキスの含有量が上記範囲を外れたもの
では乳酸発酵の発酵効率が悪く、得られる発酵液
乃至発酵母液も香味に劣る。麦芽エキスに、乳酸
菌の栄養要求物質的なものとしてホエーの蛋白分
解酵素処理物を利用し、また得られる発酵母液へ
飲用に優れた旨味、こく、まろやかさ等を付与す
る副材としてホエーの蛋白分解酵素処理物を利用
するのである。
In the present invention, a mixed solution of malt extract and whey treated with a proteolytic enzyme as described above, which contains 30 to 60% (W/V) of the malt extract, is subjected to lactic acid fermentation. Even if it is a malt extract alone, a whey proteolytic enzyme-treated product alone, or even a mixed solution of malt extract and whey proteolytic enzyme-treated product, if the malt extract content is outside the above range, lactic acid fermentation will occur. The efficiency is poor, and the resulting fermentation liquid or fermentation mother liquor is inferior in flavor. In the malt extract, we use proteolytic enzyme-treated whey as a substance required for nutrition by lactic acid bacteria, and we also use whey protein as an adjunct to give the resulting fermentation mother liquor excellent flavor, body, and mellowness. The enzyme-treated product is used.

第1図は、麦芽エキス(三共フーズ社製、三共
モルトB2)の40%(W/V)水溶液単品系と、
該水溶液80容量部及びホエーの蛋白分解酵素処理
物[粉末状ホエーの8%(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)加えて前述の如く酵素処
理したものの遠心分離液]20容量部混合系とそれ
ぞれに、予備培養したラクトバシルス・ブルガリ
カスを基質1ml当り2×106cellsとなるように加
え、37℃で静置発酵した場合の、乳酸発酵状況を
例示するグラフである(図中の滴定酸度は乳酸発
酵によつて生成した乳酸換算値、以下同じ)。ま
た第2図は、麦芽エキス(前掲のもの)の38%
(W/V)水溶液80容量部及びホエーの蛋白分解
酵素処理物[粉末状ホエーの12%(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)加えて前述の如く
酵素処理したものの遠心分離液]20容量部混合系
に、予備培養したラクトバシルス・ブリガリカス
を基質1ml当り4×106cellsとなるように加え、
37℃で静置発酵した場合の、乳酸発酵状況を例示
するグラフである。この第1図及び第2図からも
明らかなように、本発明における麦芽エキスとホ
エーの蛋白分解酵素処理物との混合溶液の乳酸発
酵が、麦芽エキス単品の場合に比べ極めて効率的
に行なわれていることが判る。
Figure 1 shows a single 40% (W/V) aqueous solution system of malt extract (Sankyo Foods Co., Ltd., Sankyo Malt B 2 ),
80 parts by volume of the aqueous solution and the proteolytic enzyme-treated whey [0.15% (W/V) of protease (Protease Amano A, manufactured by Amano Pharmaceutical Co., Ltd.) was added to an 8% (W/V) aqueous solution of powdered whey, and the above-mentioned [Centrifuged liquid of enzyme-treated product] 20 volumes of mixed system and pre-cultured Lactobacillus bulgaricus were added to each 2 x 10 6 cells per ml of substrate, and fermented statically at 37°C. This is a graph illustrating the state of lactic acid fermentation (the titratable acidity in the figure is the equivalent value of lactic acid produced by lactic acid fermentation; the same applies hereinafter). Figure 2 shows 38% of the malt extract (mentioned above).
(W/V) 80 parts by volume of aqueous solution and proteolytic enzyme-treated whey [12% (W/V) aqueous solution of powdered whey with 0.20% (W/V) of protease (Protease Amano P manufactured by Amano Pharmaceutical Co., Ltd.) In addition, add pre-cultured Lactobacillus brigaricus to 20 volumes of the centrifuged solution treated with the enzyme as described above at a concentration of 4 x 10 6 cells per 1 ml of substrate.
It is a graph illustrating the lactic acid fermentation situation in the case of static fermentation at 37°C. As is clear from FIGS. 1 and 2, the lactic acid fermentation of the mixed solution of malt extract and whey treated with proteolytic enzymes in the present invention is extremely efficient compared to the case of malt extract alone. It can be seen that

第3図は、ホエーの蛋白分解酵素処理物[粉末
状ホエーの10%(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0.15
%加えて前述の如く処理したものの遠心分離液]
20容量部を含む100容量部の水溶液へ麦芽エキス
(前掲のもの)を10〜70%(W/V)となるよう
に加えた7種の混合系がそれぞれに、予備培養し
たラクトバシルス・ブリガリカスを基質1ml当り
1×106cellsとなるように加え、37℃で静置発酵
した場合の、乳酸発酵状況を例示するグラフであ
る。この第3図からも明らかなように、乳酸発酵
基質となる麦芽エキスとホエーの蛋白分解酵素処
理物との混合溶液における麦芽エキスの濃度(い
ずれもW/V表示)が30〜60%の範囲で、他の10
%、20%及び7%よりも乳酸発酵が効率的であ
る。そして、少なくも10%や20%の低濃度に比
べ、30〜60%の高濃度で麦芽エキスを含む混合溶
液を乳酸発酵させれば、得られる発酵母液もそれ
だけ高濃度になり、したがつてそれだけ該発酵母
液の保存等取扱いが容易になつて、該発酵母液か
らの各種製品への展開も容易になる。本発明にお
いて、麦芽エキスとホエーの蛋白分解酵素処理物
との混合溶液中の麦芽エキスの濃度を30〜60%
(W/V)にする由縁である。そしてまた、この
ような乳酸発酵状況の下に、得られる発酵母液を
2点嗜好又は3点嗜好順位法で官能評価した1%
危険率の有意差検定結果を対比すると、麦芽エキ
スとホエーの蛋白分解酵素処理物との混合溶液中
におけるこれらの割合(重量比)が、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の範囲において、乳酸発酵がよ
り効率的に行なわれ且つ得られる発酵母液もより
飲用に優れた複合的香味を有するのである。
Figure 3 shows whey treated with protease [protease (Protease Amano P, manufactured by Amano Pharmaceutical Co., Ltd.) at 0.15% in a 10% (W/V) aqueous solution of powdered whey.
% and the centrifuged solution treated as described above]
Seven types of mixed systems in which malt extract (as listed above) was added to 100 parts by volume of an aqueous solution containing 20 parts by volume at a concentration of 10 to 70% (W/V) were used to incubate pre-cultured Lactobacillus brigaricus. It is a graph illustrating the lactic acid fermentation situation when the substrate is added at 1×10 6 cells per ml and fermented statically at 37°C. As is clear from Fig. 3, the concentration of malt extract (all expressed in W/V) in the mixed solution of malt extract, which serves as a lactic acid fermentation substrate, and whey proteolytic enzyme-treated product is in the range of 30 to 60%. And the other 10
%, 20% and 7%, lactic acid fermentation is more efficient. If a mixed solution containing malt extract is subjected to lactic acid fermentation at a high concentration of 30 to 60% compared to a low concentration of at least 10% or 20%, the concentration of the fermentation mother liquor obtained will be that much higher, and therefore, This makes it easier to store and handle the fermentation mother liquor, and it also becomes easier to develop various products from the fermentation mother liquor. In the present invention, the concentration of malt extract in the mixed solution of malt extract and whey proteolytic enzyme-treated product is adjusted to 30 to 60%.
This is the reason for making it (W/V). Under such lactic acid fermentation conditions, the fermentation mother liquor obtained was sensory evaluated using the 2-point preference or 3-point preference ranking method.
Comparing the results of the significant difference test of the risk ratio, we can see that the ratio (weight ratio) of malt extract and whey proteolytic enzyme-treated product in a mixed solution of malt extract/whey proteolytic enzyme-treated product (solid equivalent )
=5/1 to 40/1, lactic acid fermentation is carried out more efficiently and the resulting fermentation mother liquor has a complex flavor that is more drinkable.

具体的に乳酸発酵は、麦芽エキスとホエーの蛋
白分解酵素処理物との混合溶液であつて該麦芽エ
キスを30〜60%(W/V)含有する混合溶液を、
例えば重炭酸ナトリウムの如きアルカリ剤でPH
6.8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、予備培養した乳酸菌を加え
て行なう。ここで使用する乳酸菌は、ラクトバシ
ルス・ブリガリカス(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)等の如き一般食品利用の乳酸菌であり、
これらは2種以上の乳酸菌を共生させることによ
つて一層好ましい乳酸発酵をさせることもでき
る。かかる菌体の添加量は、乳酸菌の性質、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1×106cellsを目標とする。発酵中
は外部からの雑菌汚染を厳重防止し、発酵温度は
25〜40℃に維持するのが好ましいが、37℃近傍が
特に好ましい。発酵温度が低すぎると、乳酸発酵
に長時間を要し、逆に発酵温度が高すぎると、乳
酸菌の増殖が速くなりすぎて、得られる発酵母液
の香味が悪い。37℃近傍での乳酸発酵は12〜24時
間で終了する。
Specifically, lactic acid fermentation involves using a mixed solution of malt extract and a proteolytic enzyme-treated whey product containing 30 to 60% (W/V) of the malt extract.
For example, use an alkaline agent such as sodium bicarbonate to
After adjusting the temperature to about 6.8 and heat sterilizing it to a temperature of about 95℃, pre-cultured lactic acid bacteria are added to the cooled mixture. The lactic acid bacteria used here are Lactobacillus brigaricus
bulugaricus), Streptococcus thermophilus, Bifidobacterium longum
lactic acid bacteria used in general foods such as
By allowing two or more types of lactic acid bacteria to coexist, more preferable lactic acid fermentation can be achieved. The amount of such bacterial cells added depends on the properties and activity of the lactic acid bacteria, the desired quality of the fermented liquid, etc., but approximately:
Aim for 1×10 6 cells per ml of substrate. During fermentation, strict prevention of bacterial contamination from outside is carried out, and the fermentation temperature is
It is preferable to maintain the temperature at 25 to 40°C, and particularly preferably around 37°C. If the fermentation temperature is too low, lactic acid fermentation will take a long time; if the fermentation temperature is too high, the lactic acid bacteria will multiply too quickly, resulting in poor flavor of the fermented mother liquor. Lactic acid fermentation at around 37°C is completed in 12 to 24 hours.

かくして得られる発酵母液は、ここに含まれる
菌体それ自身も有用であるため、菌体を含有した
ままで、又は菌体を濾過や遠心分離で除去した後
に、適宜水希釈して調整し、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。製品化最終段階において、糖類や香料等の可
溶性成分を加えると、より飲用し易くなる。また
カーボネーシヨンすると、さわやかな乳酸発酵飲
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 fermentation mother liquor obtained in this way is useful as a result of the bacteria contained therein, so it can be prepared either while containing the bacteria or after the bacteria have been removed by filtration or centrifugation, and then diluted with water as appropriate. into products (e.g. chilled products, or regular bottled or canned products after sterilization). Adding soluble ingredients such as sugars and flavorings at the final stage of product production makes it easier to drink. When carbonated, a refreshing lactic acid fermented beverage can be obtained. The carbonation in this case is
It is preferable that the carbon dioxide volume in the product is about 2.0 to 2.5.

かくして得られる乳酸発酵飲料は、原料である
麦芽エキスとホエーの蛋白分解酵素処理物とにそ
れぞれ含まれる各種のミネラル及びビタミン等と
該ホエーの蛋白分解酵素処理によつて富化した各
種のアミノ酸及び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、本
発明によつて得られる乳酸発酵飲料と、他の諸条
件を同一にして得られる麦芽エキス単品系やホエ
ーの蛋白分解酵素処理物単品系等の乳酸発酵飲料
等とを官能評価すると、1%の危険率で、本発明
によつて得られる乳酸発酵飲料に好結果が有意検
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)。
The lactic acid fermented beverage thus obtained contains various minerals and vitamins contained in the malt extract and the proteolytic enzyme-treated whey, respectively, and various amino acids and vitamins enriched by the proteolytic enzyme treatment of the whey. Peptides, etc. are utilized, and it has a complex flavor that is excellent for drinking. In fact, a sensory evaluation of the lactic acid fermented beverage obtained by the present invention and lactic acid fermented beverages such as a single malt extract system and a single system of whey proteolytic enzyme-treated products obtained under the same conditions revealed that At a risk rate of 1%, a positive result for the lactic acid fermented beverage obtained by the present invention can be significantly tested (20 inspectors x 3 repetitions x
2-point or 3-point 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、処理液を遠心分離液したもの]20容量部との
混合溶液を、重炭酸ナトリウムでPH6.8に調整し、
これを95℃達温で加熱殺菌して37℃に冷却した
後、予備培養したラクトバシルス・ブリガリカス
を基質1ml当り3×106cellsとなるように加え、
外部からの菌的汚染を防止しつつ、37℃で20時間
静置培養した。得られた発酵液のPH4.01、滴定酸
度200mg%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.)] 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 volumes was adjusted to pH 6.8 with sodium bicarbonate,
After heating and sterilizing this at a temperature of 95°C and cooling it to 37°C, pre-cultured Lactobacillus brigaricus was added at a density of 3 x 10 6 cells per ml of substrate.
Static culture was performed at 37°C for 20 hours while preventing bacterial contamination from the outside. The resulting fermentation liquid had a pH of 4.01 and a titratable acidity of 200 mg%. 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500g+香料(レモン系)1gの割合で調
整した後、95℃達温で加熱殺菌して10℃に冷却
し、乳酸発酵飲料(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 + 500 g of sugar + 1 g of fragrance (lemon type), the mixture was heat sterilized at 95°C and cooled to 10°C to produce a lactic acid fermented beverage (Example).

他の諸条件を同一にしつつ並行して、麦芽エキ
ス単品系の乳酸発酵飲料(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
に好結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 malt extract-based lactic acid fermented beverage (comparative example) was manufactured in parallel with other conditions being the same, but when the sensory evaluation of the example and the comparative example was performed, a significant result was found that the example had a better result. (20 inspectors x 2 repetitions x 2 preferences 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 A 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500g+香料(柑橘系)1gの割合で調整
し、そのままチルド(5℃)の乳酸発酵飲料(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.) lactic acid fermented beverage (Example) was prepared by adjusting the ratio of +500g sugar +1g 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 A 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乳酸発酵飲料(実施
例)を製造した。
Then, the fermentation mother liquor was diluted 3 times with water, then adjusted in the same manner as in Example 1, heat sterilized, cooled (5°C), and centrifuged, followed by carbonation with a target carbon dioxide volume of 2.3 to make a lactic acid 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.

<発明の効果> 既に明らかなように、以上説明した本発明に
は、効率的な乳酸発酵によつて飲用に優れた香味
を有する乳酸発酵飲料を製造することができ、ま
た高濃度の発酵母液を得るため、保存等取扱いや
各種製品への展開が容易になるという効果があ
る。
<Effects of the Invention> As is already clear, the present invention described above makes it possible to produce a lactic acid-fermented beverage having an excellent drinkable flavor through efficient lactic acid fermentation, and to produce a fermented mother liquor with a high concentration. This has the effect of facilitating storage, handling, and development into various products.

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

第1図は本発明における乳酸発酵状況を例示す
るグラフ(但し、図中単品系は比較例)、第2図
と第3図は本発明における他の各別の乳酸発酵状
況を例示するグラフである(但し、第3図中10
%、20%、70%は比較例)。
Figure 1 is a graph illustrating the lactic acid fermentation situation in the present invention (however, the single product system in the figure is a comparative example), and Figures 2 and 3 are graphs illustrating each other lactic acid fermentation status in the present invention. Yes (however, 10 in Figure 3)
%, 20%, and 70% are comparative examples).

Claims (1)

【特許請求の範囲】 1 麦芽エキスとホエーの蛋白分解酵素処理物と
の混合溶液であつて該麦芽エキスを30〜60%
(W/V)含有する混合溶液をPH調整し、殺菌し
て冷却した後、予備培養した乳酸菌を加えて乳酸
発酵することにより発酵母液を得、該発酵母液を
水希釈して調整することを特徴とする乳酸発酵飲
料の製造方法。 2 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
溶液を用いる特許請求の範囲第1項記載の乳酸発
酵飲料の製造方法。
[Claims] 1. A mixed solution of malt extract and whey treated with a proteolytic enzyme, the malt extract containing 30 to 60%.
After adjusting the pH of the mixed solution containing (W/V), sterilizing it and cooling it, pre-cultured lactic acid bacteria are added and fermented with lactic acid to obtain a fermentation mother liquor, and the fermentation mother liquor is diluted with water for adjustment. Characteristic method for producing lactic acid fermented beverages. 2. The method for producing a lactic acid fermented beverage according to claim 1, using a mixed solution of malt extract/whey treated with a proteolytic enzyme (in terms of solid matter) = 5/1 to 40/1 (weight ratio).
JP9522583A 1983-05-30 1983-05-30 Lactic acid fermentation beverage and production thereof Granted JPS59220153A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9522583A JPS59220153A (en) 1983-05-30 1983-05-30 Lactic acid fermentation beverage and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9522583A JPS59220153A (en) 1983-05-30 1983-05-30 Lactic acid fermentation beverage and production thereof

Publications (2)

Publication Number Publication Date
JPS59220153A JPS59220153A (en) 1984-12-11
JPH04615B2 true JPH04615B2 (en) 1992-01-08

Family

ID=14131806

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9522583A Granted JPS59220153A (en) 1983-05-30 1983-05-30 Lactic acid fermentation beverage and production thereof

Country Status (1)

Country Link
JP (1) JPS59220153A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6375844A (en) * 1986-09-18 1988-04-06 Fujitsu Ltd Trouble recovery confirming system
JPH0640796B2 (en) * 1986-12-26 1994-06-01 不二製油株式会社 Lactic acid fermented product manufacturing method
DE102009019525A1 (en) * 2009-04-30 2010-11-11 Nordmann Marken Holding Gmbh Simplified fermentative production of soft drinks

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54129164A (en) * 1978-03-27 1979-10-06 Kansai Runa Kk Production of lactic acid beverage
CH635483A5 (en) * 1978-12-04 1983-04-15 Nestle Sa Process for the manufacture of a drink with yoghurt taste
JPS5737315A (en) * 1980-08-18 1982-03-01 Nippon Telegr & Teleph Corp <Ntt> Connection part of submarine optical cable

Also Published As

Publication number Publication date
JPS59220153A (en) 1984-12-11

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