JP2003070462A - LACTOBACILLUS WITH ABILITY TO PRODUCE 7%. gamma-AMINOBUTYRIC ACID, AND METHOD FOR PRODUCING FOOD USING THE LACTOBACILLUS - Google Patents

LACTOBACILLUS WITH ABILITY TO PRODUCE 7%. gamma-AMINOBUTYRIC ACID, AND METHOD FOR PRODUCING FOOD USING THE LACTOBACILLUS

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Publication number
JP2003070462A
JP2003070462A JP2001268696A JP2001268696A JP2003070462A JP 2003070462 A JP2003070462 A JP 2003070462A JP 2001268696 A JP2001268696 A JP 2001268696A JP 2001268696 A JP2001268696 A JP 2001268696A JP 2003070462 A JP2003070462 A JP 2003070462A
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Japan
Prior art keywords
aminobutyric acid
food
acid
fermented
strain
Prior art date
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Application number
JP2001268696A
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Japanese (ja)
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JP3880820B2 (en
Inventor
Kiyoshi Hayakawa
潔 早川
Yoshie Ueno
義栄 上野
Shinji Azumaguchi
伸二 東口
Busaku Kin
武祚 金
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PHARMAFOODS KENKYUSHO KK
Pharma Foods Research Co Ltd
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PHARMAFOODS KENKYUSHO KK
Pharma Foods Research Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a method for producing γ-aminobutyric acid-rich food. SOLUTION: The food, i.e., a fermented product containing γ-aminobutyric acid is obtained by inoculating a fermentation raw material containing glutamic acid or a salt thereof with a Lactobacillus hilgardii K-3 strain (FERM P-18422) isolated from kimchi (a type of Korean pickles) and then culturing the thus isolated K-3 strain.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、グルタミン酸を
グルタミン酸脱炭酸酵素(グルタミン酸デカルボキシラ
ーゼ)の作用により脱炭酸してγ−アミノ酪酸(GAB
A)を生成するγ−アミノ酪酸生産能を有する乳酸菌、
ならびに、その乳酸菌を使用してγ−アミノ酪酸を含有
する食品を製造する方法に関するものである。
TECHNICAL FIELD The present invention relates to decarboxylation of glutamic acid by the action of glutamate decarboxylase (glutamate decarboxylase) to produce γ-aminobutyric acid (GAB
A) a lactic acid bacterium capable of producing γ-aminobutyric acid,
It also relates to a method for producing a food containing γ-aminobutyric acid using the lactic acid bacterium.

【0002】[0002]

【従来の技術】γ−アミノ酪酸は、ギャバとも呼ばれ、
自然界に広く分布している非タンパク質アミノ酸の1種
であり、食品の成分としても、茶、野菜類、穀類などに
普通に含まれている。生体内においては、グルタミン酸
が脱炭酸されて生成され、人体では特に、脳内の黒質、
大脳基底核、視床下部等に高濃度に存在していることが
分かっている。
2. Description of the Related Art γ-Aminobutyric acid is also called GABA,
It is a type of non-protein amino acid widely distributed in nature, and is commonly contained in foods such as tea, vegetables, and cereals. In the living body, glutamic acid is decarboxylated and produced, and in the human body, especially in the substantia nigra in the brain,
It is known to be present in high concentrations in the basal ganglia, hypothalamus, etc.

【0003】γ−アミノ酪酸の生理作用としては、血管
を拡張して血圧を下げることが良く知られている。ま
た、γ−アミノ酪酸は、脳内の血液の流れを活発にし、
脳細胞への酸素供給量を増加させて、代謝機能を促進さ
せる働きがあり、主要な抑制性の神経伝達物質として中
枢神経系において重要な役割を果たしている。そして、
医薬品としては、脳血管の狭窄や閉塞による頭痛、耳鳴
りなどの治療に応用されている。また、γ−アミノ酪酸
の人体への投与が、学習能力の増強や長期記憶の促進に
貢献することも報告されている。
As a physiological action of γ-aminobutyric acid, it is well known that blood vessels are expanded to lower blood pressure. In addition, γ-aminobutyric acid activates blood flow in the brain,
It functions to increase the oxygen supply to brain cells and promote metabolic functions, and plays an important role in the central nervous system as a major inhibitory neurotransmitter. And
As a drug, it has been applied to the treatment of headache, tinnitus, etc. due to stenosis or blockage of cerebral blood vessels. It has also been reported that administration of γ-aminobutyric acid to the human body contributes to enhancement of learning ability and promotion of long-term memory.

【0004】したがって、γ−アミノ酪酸を食品として
摂取すれば、上記の生理作用が期待されることから、適
当な処理を食品に施すことにより、γ−アミノ酪酸の含
有量を増加させた食品もいくつか提唱されている。例え
ば、米などの胚芽を水に浸漬処理した食品素材(特許第
2810993号公報)や、茶葉を嫌気処理したギャバ
ロン茶(実開昭63−103285号公報)などが知ら
れている。
Therefore, if γ-aminobutyric acid is ingested as a food, the above-mentioned physiological action is expected. Therefore, a food having an increased γ-aminobutyric acid content can be obtained by subjecting the food to an appropriate treatment. Some have been proposed. For example, known are food materials obtained by dipping embryos such as rice in water (Japanese Patent No. 2810993) and gabaron tea obtained by anaerobically treating tea leaves (Japanese Utility Model Publication No. 63-103285).

【0005】一方、食品用の微生物を利用したγ―アミ
ノ酪酸含有食品の製造方法として、ラクトバチルス(L
actobacillus)属の乳酸菌を用いたもの
(特許第2704493号公報、特開2000−308
457号公報、特開2000−210075号公報等)
や麹菌を用いたもの(特開平10−165191号公
報、特開平11−103825号公報等)、酵母または
クロレラを用いたもの(特開平9−238650号公
報)など、多数の報告がある。
On the other hand, as a method for producing γ-aminobutyric acid-containing foods using food-use microorganisms, Lactobacillus (L
Those using lactic acid bacteria of the genus actobacillus (Japanese Patent No. 2704493, JP 2000-308A).
No. 457, JP 2000-210075, etc.)
There are many reports such as those using yeast and koji molds (JP-A-10-165191, JP-A-11-103825, etc.) and those using yeast or chlorella (JP-A-9-238650).

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記し
た従来の方法によりγ−アミノ酪酸の含有量を増加させ
た食品は、処理を施す前に比べて含有量が多くなっては
いるが、食品100g当たりのγ−アミノ酪酸の含有量
は1000mg未満、すなわち食品中の含有割合は1%
にも満たない。この程度の含有割合では、例えば、γ−
アミノ酪酸を含有するそれらの食品をスープ、惣菜、漬
物、菓子などの食物や飲料に添加し、加工食品の原材料
とするなどして幅広く利用するためには、まだ不十分で
ある。
However, the food having an increased γ-aminobutyric acid content by the above-mentioned conventional method has a higher content than that before the treatment, but 100 g of the food The content of γ-aminobutyric acid per unit is less than 1000 mg, that is, the content rate in food is 1%
Less than With this content ratio, for example, γ-
It is still insufficient to add such foods containing aminobutyric acid to foods and drinks such as soups, prepared foods, pickles and confectionery and to use them widely as raw materials for processed foods.

【0007】この発明は、以上のような事情に鑑みてな
されたものであり、γ−アミノ酪酸を高い割合で含有す
る食品を得ることができるγ−アミノ酪酸生産能を有す
る乳酸菌を提供すること、ならびに、その乳酸菌を使用
してγ−アミノ酪酸を高い割合で含有する食品を製造す
ることができる食品の製造方法を提供することを目的と
する。
The present invention has been made in view of the above circumstances, and provides a lactic acid bacterium having a γ-aminobutyric acid-producing ability, which can obtain a food containing a high proportion of γ-aminobutyric acid. It is also an object of the present invention to provide a method for producing a food which can produce a food containing a high proportion of γ-aminobutyric acid using the lactic acid bacterium.

【0008】[0008]

【課題を解決するための手段】本発明者は、発酵・醸造
食品を対象として高いγ−アミノ酪酸生成能を有する乳
酸菌の検索を行ってきた結果、キムチより単離したラク
トバチルス・ヒルガルディー(Lactobacill
us hilgardii)に属する菌株が高いγ―ア
ミノ酪酸生産能を有しており、その菌株を使用し、例え
ば10重量%のグルタミン酸ナトリウムを含む培養液で
その菌株を培養させれば、約5重量%の高濃度のγ―ア
ミノ酪酸を含む培養液が得られること、また、その培養
液を濾過し濃縮するだけで15重量%以上のγ−アミノ
酪酸を含有する発酵液が得られることを見い出して、本
発明を完成するに至った。
Means for Solving the Problems The present inventor has conducted a search for lactic acid bacteria having a high γ-aminobutyric acid-producing ability in fermented and brewed foods, and as a result, Lactobacillus hirugardei (Lactobacillus) isolated from kimchi was found.
A strain belonging to us hirgardii) has a high ability to produce γ-aminobutyric acid, and if the strain is used and is cultivated in a culture solution containing 10 wt% sodium glutamate, for example, about 5 wt% It was found that a culture broth containing a high concentration of γ-aminobutyric acid was obtained, and that a fermentation broth containing 15% by weight or more of γ-aminobutyric acid was obtained simply by filtering and concentrating the culture. The present invention has been completed.

【0009】すなわち、請求項1に係る発明は、γ―ア
ミノ酪酸生産能を有する乳酸菌において、キムチから単
離された菌株であって、培地にグルタミン酸またはその
塩類を添加することにより増殖が促進されてグルタミン
酸脱炭酸酵素の作用によりγ―アミノ酪酸を生成するラ
クトバチルス・ヒルガルディーに属する菌株であること
を特徴とする。
That is, the invention according to claim 1 is a lactic acid bacterium capable of producing γ-aminobutyric acid, which is a strain isolated from kimchi and whose growth is promoted by adding glutamic acid or a salt thereof to the medium. It is characterized by being a strain belonging to Lactobacillus hirugardi that produces γ-aminobutyric acid by the action of glutamate decarboxylase.

【0010】請求項2に係る発明は、請求項1記載の乳
酸菌において、前記菌株がラクトバチルス・ヒルガルデ
ィーK−3株 FERM P−18422(以下、単に
「K−3株」という)であることを特徴とする。
The invention according to claim 2 is the lactic acid bacterium according to claim 1, wherein the strain is Lactobacillus hilgardi K-3 strain FERM P-18422 (hereinafter simply referred to as "K-3 strain"). Characterize.

【0011】請求項3に係る発明は、γ―アミノ酪酸生
産能を有する乳酸菌を使用した食品の製造方法におい
て、グルタミン酸またはその塩類を含有する発酵原料
に、請求項1または請求項2記載の乳酸菌を接種し培養
して、γ−アミノ酪酸を含有する発酵物を得ることを特
徴とする。
The invention according to claim 3 is a method for producing a food using a lactic acid bacterium capable of producing γ-aminobutyric acid, wherein the fermentation raw material containing glutamic acid or a salt thereof is added to the lactic acid bacterium according to claim 1 or 2. Is inoculated and cultured to obtain a fermented product containing γ-aminobutyric acid.

【0012】請求項4に係る発明は、請求項3記載の製
造方法において、初発pH4.5〜5.5で発酵処理を
行うことを特徴とする。このようにすると、乳酸菌は、
その増殖が最も促進され、γ−アミノ酪酸を生産する能
力が向上する。
The invention according to claim 4 is characterized in that, in the manufacturing method according to claim 3, the fermentation treatment is carried out at an initial pH of 4.5 to 5.5. In this way, the lactic acid bacteria
Its growth is most promoted and its ability to produce γ-aminobutyric acid is improved.

【0013】請求項5に係る発明は、請求項3または請
求項4記載の製造方法において、前記発酵物が発酵液で
あり、その発酵液を濾過、濃縮および乾燥させて、γ−
アミノ酪酸を含有する粉末を得ることを特徴とする。
The invention according to claim 5 is the method according to claim 3 or 4, wherein the fermented product is a fermented liquid, and the fermented liquid is filtered, concentrated and dried to obtain γ-.
It is characterized in that a powder containing aminobutyric acid is obtained.

【0014】請求項6に係る発明は、請求項3または請
求項4記載の製造方法において、前記発酵物が発酵液で
あり、その発酵液を濃縮した後に食物または飲料に添加
して、γ−アミノ酪酸を含有する飲食物を得ることを特
徴とする。
According to a sixth aspect of the present invention, in the production method according to the third or fourth aspect, the fermented product is a fermented liquor, and the fermented liquor is concentrated and then added to food or beverage to obtain γ- A feature is to obtain a food or drink containing aminobutyric acid.

【0015】請求項7に係る発明は、請求項5記載の製
造方法において、前記粉末を食物または飲料に添加し
て、γ−アミノ酪酸を含有する飲食物を得ることを特徴
とする。
The invention according to claim 7 is characterized in that, in the manufacturing method according to claim 5, the powder is added to food or beverage to obtain a food or drink containing γ-aminobutyric acid.

【0016】[0016]

【発明の実施の形態】以下、この発明の好適な実施形態
について説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Preferred embodiments of the present invention will be described below.

【0017】この発明に係る乳酸菌は、キムチから単離
されたラクトバチルス・ヒルガルディーに属する菌株で
あり、培地にグルタミン酸またはその塩類を添加するこ
とにより増殖が促進されてグルタミン酸脱炭酸酵素の作
用によりγ―アミノ酪酸を高率で生成する能力を有す
る。すなわち、このキムチ由来の乳酸菌は、1L中に1
00gのグルタミン酸ナトリウムを含む液体培地におい
て、30℃の温度で48時間培養したとき、γ―アミノ
酪酸を45g/L以上生産することができる。この乳酸
菌は、K−3株であることが望ましい。
The lactic acid bacterium according to the present invention is a strain belonging to Lactobacillus hilgardi isolated from Kimchi, and its growth is promoted by the addition of glutamic acid or its salts to the medium. -It has the ability to produce aminobutyric acid at a high rate. That is, this kimchi-derived lactic acid bacterium has 1
When cultured in a liquid medium containing 00 g of sodium glutamate at a temperature of 30 ° C. for 48 hours, 45 g / L or more of γ-aminobutyric acid can be produced. The lactic acid bacterium is preferably the K-3 strain.

【0018】乳酸菌をキムチから単離するのは、次のよ
うな方法による。すなわち、キムチにグルタミン酸ナト
リウムを10g/kg添加して発酵熟成させたものを分
離源とし、乳酸菌分離用のBCP加プレートカウントア
ガール培地(ニッスイ(株)製)を用いて乳酸菌を分離
し、分離菌を10g/Lのグルタミン酸ナトリウムを含
有したGYP液体培地で培養して、γ―アミノ酪酸の生
成量の多い菌株を選抜した。
The lactic acid bacterium is isolated from kimchi by the following method. That is, kimchi was added with 10 g / kg of sodium glutamate and fermented and matured as a separation source, and lactic acid bacteria were separated using a BCP-added plate count agar medium (manufactured by Nissui Co., Ltd.) for separating lactic acid bacteria. Was cultured in a GYP liquid medium containing 10 g / L of sodium glutamate, and a strain having a large production amount of γ-aminobutyric acid was selected.

【0019】上記したようにして単離されたK−3株の
菌学的性質を表1に示す。
Table 1 shows the mycological properties of the K-3 strain isolated as described above.

【表1】 [Table 1]

【0020】上記したキムチ由来の乳酸菌を使用し、グ
ルタミン酸またはその塩類を含有する発酵原料に乳酸菌
を接種し培養して、γ−アミノ酪酸を含有する発酵食品
を製造する。乳酸菌としては、キムチから単離培養さ
れ、継代培養されたものが使用されるが、キムチに含ま
れている同種の乳酸菌をそのままであるいは新たに単離
して用いるようにしてもよい。また、凍結乾燥菌体、凍
結保存株および液体培養液のうちのいずれを使用しても
よいが、使用の前日から1%以上のグルタミン酸を含む
発酵液または液体培地で前培養したものを使用すること
が好ましい。
Using the lactic acid bacterium derived from kimchi described above, a fermentation raw material containing glutamic acid or a salt thereof is inoculated with the lactic acid bacterium and cultured to produce a fermented food containing γ-aminobutyric acid. As the lactic acid bacterium, a lactic acid bacterium isolated and cultured from Kimchi and subcultured is used, but the same lactic acid bacterium contained in Kimchi may be used as it is or may be newly isolated and used. Also, any of freeze-dried cells, cryopreserved strains and liquid culture medium may be used, but the one pre-cultured in a fermentation liquid or liquid medium containing 1% or more glutamic acid from the day before use is used. It is preferable.

【0021】この発酵食品の製造方法で用いるグルタミ
ン酸は、化学的にはアミノ酸の一種であるL−グルタミ
ン酸を指し、調味料としての用途を持つ食品添加物であ
るグルタミン酸やグルタミン酸ナトリウム、その他のグ
ルタミン酸塩、さらに食品蛋白質を酸や酵素で加水分解
して得られるグルタミン酸のいずれを用いても構わな
い。また、調味料、水産加工品、トマトなど、遊離グル
タミン酸を含む食品をそのままで用いても構わない。た
だし、より多量のγ−アミノ酪酸を含有した食品を得よ
うとする場合には、より多量のグルタミン酸を含有する
発酵原料を用いることが必要である。
Glutamic acid used in this method for producing fermented foods chemically refers to L-glutamic acid, which is one of the amino acids, and is a food additive such as glutamic acid, sodium glutamate, and other glutamate which has a use as a seasoning. Further, any of glutamic acid obtained by hydrolyzing food protein with acid or enzyme may be used. Further, foods containing free glutamic acid such as seasonings, processed marine products and tomatoes may be used as they are. However, in order to obtain a food containing a larger amount of γ-aminobutyric acid, it is necessary to use a fermentation raw material containing a larger amount of glutamic acid.

【0022】また、発酵培地は、乳酸菌の生育のため
に、上記したグルタミン酸の他に、ブドウ糖、果糖、麦
芽糖などの糖質や、酵母エキス、肉エキス等のビタミン
やミネラルを含む食品を含有することが好ましい。さら
に、乳化剤や安定剤、pH調整剤などの食品添加物を用
いても構わない。
The fermentation medium contains foods containing glucose such as glucose, fructose and maltose, and vitamins and minerals such as yeast extract and meat extract in addition to the above-mentioned glutamic acid for the growth of lactic acid bacteria. It is preferable. Further, food additives such as emulsifiers, stabilizers and pH adjusters may be used.

【0023】発酵処理に使用される容器は、洗浄や加熱
殺菌を行うことができて、食品の製造に使用可能である
容器であれば、大きさや材質を問わないが、雑菌が混入
しにくい構造をしたものが好ましい。
The container used for fermentation treatment can be washed and sterilized by heating and can be used for food production, regardless of size or material, but a structure in which various bacteria are not easily mixed. Those having the above are preferable.

【0024】発酵処理の条件は、次の通りである。すな
わち、発酵温度は、好ましくは20℃〜30℃で、発酵
時間は、例えば48時間〜75時間であり、初発pH
は、4.0〜7.0が好ましい。但し、5重量%以上の
高濃度のグルタミン酸ナトリウムを含む発酵培地を用い
て発酵させる場合は、菌の増殖が最も促進される初発p
H4.5〜5.5が最も好ましい。例えば、4重量%の
グルタミン酸ナトリウムを含むGYP液体培地でK−3
株を培養させた場合、72時間後のγ―アミノ酪酸の生
成量は、初発pH6.3および初発pH5.0のいずれ
においても約2重量%であったのに対し、10重量%の
グルタミン酸ナトリウムを含むGYP液体培地でK−3
株を培養させた場合には、72時間後のγ―アミノ酪酸
の生成量は、初発pH6.3では約3重量%であるのに
対し、初発pH5.0では約5重量%に達した。また、
発酵液のpHは、K−3株の増殖に伴って上昇し、発酵
処理を開始してから24時間〜48時間経過した時点で
はpH7〜8の中性域に達する。このため、発酵処理を
開始してから24時間前後経過した時点で、発酵液を再
びpH5程度に調整して発酵処理を続けるようにする。
このようにすることにより、乳酸菌の増殖をさらに促進
させ、γ−アミノ酪酸生成の速度や効率を上昇させるこ
とができる。
The conditions of fermentation treatment are as follows. That is, the fermentation temperature is preferably 20 ° C to 30 ° C, the fermentation time is, for example, 48 hours to 75 hours, and the initial pH is
Is preferably 4.0 to 7.0. However, when fermentation is performed using a fermentation medium containing a high concentration of 5% by weight or more of sodium glutamate, the initial p
Most preferred is H4.5-5.5. For example, K-3 in a GYP liquid medium containing 4% by weight of sodium glutamate.
When the strain was cultured, the amount of γ-aminobutyric acid produced after 72 hours was about 2% by weight at both the initial pH of 6.3 and the initial pH of 5.0, whereas 10% by weight of sodium glutamate was used. K-3 in GYP liquid medium containing
When the strain was cultured, the amount of γ-aminobutyric acid produced after 72 hours was about 3% by weight at the initial pH of 6.3, while it reached about 5% by weight at the initial pH of 5.0. Also,
The pH of the fermented liquor rises with the growth of the K-3 strain, and reaches a neutral range of pH 7 to 8 when 24 hours to 48 hours have passed since the start of the fermentation treatment. Therefore, after about 24 hours have passed from the start of the fermentation process, the pH of the fermented liquid is adjusted to about 5 again to continue the fermentation process.
By doing so, the growth of lactic acid bacteria can be further promoted, and the rate and efficiency of γ-aminobutyric acid production can be increased.

【0025】乳酸菌を培養して得られたγ−アミノ酪酸
を含有する発酵液は、そのまま各種の飲料や食物に添加
するなどして用いてもよく、また、濾過、濃縮、乾燥な
どの処理工程によってγ−アミノ酪酸の含有量をさらに
高めてから利用するようにしてもよい。このようにし
て、クロマトグラフィーなどの精製工程を経なくても、
廃棄物や副産物が少なく比較的安価に実施することがで
きる方法により、γ−アミノ酪酸濃度が高く、加工食品
などの原材料などとして広い用途を持つ液体または粉末
状のγ−アミノ酪酸高含有食品を得ることができる。ま
た、濾過、濃縮、乾燥などの処理工程を経ることによ
り、多量のγ−アミノ酪酸を含有した各種の飲料や食
物、例えばγ−アミノ酪酸濃度が15重量%以上である
飲食物が得られる。
The fermented broth containing γ-aminobutyric acid obtained by culturing lactic acid bacteria may be used as it is by adding it to various beverages and foods, or may be subjected to treatment steps such as filtration, concentration and drying. Therefore, the content of γ-aminobutyric acid may be further increased before use. In this way, without going through purification steps such as chromatography,
By the method that can be carried out relatively inexpensively with little waste and by-products, liquid or powdery high γ-aminobutyric acid-rich foods that have a high concentration of γ-aminobutyric acid and have wide applications as raw materials such as processed foods. Obtainable. In addition, various kinds of beverages and foods containing a large amount of γ-aminobutyric acid, for example, foods and drinks having a γ-aminobutyric acid concentration of 15% by weight or more can be obtained by passing through treatment steps such as filtration, concentration, and drying.

【0026】上記した濾過工程は、濾紙、濾布などを用
いた通常の食品加工用の濾過設備を使用して行うことが
でき、珪藻土やセルロース、活性炭などの濾過助剤を用
いるようにしてもよい。濃縮工程は、真空濃縮機、減圧
濃縮機、蒸留釜、凍結濃縮機などの設備を用いて行う以
外にも、火にかけた鍋で発酵液中の水分を蒸発させるだ
けでもよい。また、乾燥工程は、噴霧乾燥や凍結乾燥な
ど、効率的かつ衛生的な方法により行うことが好まし
い。さらに、γ−アミノ酪酸の含有量をより高めた食品
を得るために、上記した工程以外にも、液体クロマトグ
ラフィーなどの方法を用いるようにすることもできる。
また、上記した発酵液を濃縮あるいは乾燥させることに
より、γ−アミノ酪酸を含有した液状または粉末状食品
が得られ、それらの食品を配合あるいは二次加工するこ
とにより、γ−アミノ酪酸を含有した飲料や食物が得ら
れる。
The above-mentioned filtration step can be carried out by using ordinary filtration equipment for food processing using filter paper, filter cloth and the like, and even if a filter aid such as diatomaceous earth, cellulose or activated carbon is used. Good. The concentration step may be performed using equipment such as a vacuum concentrator, a vacuum concentrator, a distillation pot, a freeze concentrator, or the like, and the water in the fermentation liquor may be simply evaporated in a pan that has been heated. The drying step is preferably performed by an efficient and hygienic method such as spray drying or freeze drying. Further, in order to obtain a food having a higher content of γ-aminobutyric acid, a method such as liquid chromatography may be used in addition to the above steps.
Further, by concentrating or drying the above-mentioned fermentation liquid, a liquid or powdery food containing γ-aminobutyric acid is obtained, and by mixing or secondary processing those foods, γ-aminobutyric acid was contained. Beverages and food are available.

【0027】また、γ−アミノ酪酸高含有食品は、上述
した成分のほかに、賦形剤、甘味料、増粘剤、タンパク
質、ペプチド、脂質、多糖類、糖質、塩類などの通常、
食品に用いられている成分を含んでいてもよい。
In addition to the above-mentioned components, foods high in γ-aminobutyric acid usually include excipients, sweeteners, thickeners, proteins, peptides, lipids, polysaccharides, sugars, salts, etc.
It may contain ingredients used in foods.

【0028】なお、得られた発酵液や発酵食品中のγ−
アミノ酪酸の含有量の測定は、高速液体クロマトグラフ
ィー、アミノ酸測定機等の分析機器や、酵素を用いた分
析試薬などを用いて行うようにすればよい。
Γ-in the obtained fermented liquid or fermented food
The content of aminobutyric acid may be measured using an analytical instrument such as high performance liquid chromatography or an amino acid measuring instrument, or an analytical reagent using an enzyme.

【0029】[0029]

【実施例】以下、この発明を適用したより具体的な実施
例について説明する。
EXAMPLES More specific examples to which the present invention is applied will be described below.

【0030】〔保存株からの復元〕凍結または凍結乾燥
の状態で長期保存しているK−3株を使用する場合は、
K−3株を滅菌水に添加して懸濁液とした後、白金耳を
用いて懸濁液を、表2に成分組成を示すGYP寒天培地
に接種し、30℃の温度で24時間、培養する。寒天培
地上に乳白色のコロニーが確認されると、そのK−3株
をそのまま以後の培養に使用することができる。K−3
株は、寒天培地上において4℃〜10℃の温度で4週
間、それを保存することができる。
[Restoration from preserved strain] When using the K-3 strain which has been stored for a long time in a frozen or freeze-dried state,
After the K-3 strain was added to sterile water to form a suspension, the suspension was inoculated using a platinum loop into a GYP agar medium having the composition shown in Table 2, and the temperature was 30 ° C. for 24 hours. Incubate. When milky white colonies are confirmed on the agar medium, the K-3 strain can be used as it is for the subsequent culture. K-3
The strain can be stored on an agar medium at a temperature of 4 ° C to 10 ° C for 4 weeks.

【0031】[0031]

【表2】 [Table 2]

【0032】〔前培養〕GYP寒天培地上のK−3株
を、白金耳を用いて5mL〜100mLのGYP液体培
地(表1に示した成分組成のGYP寒天培地から標準寒
天を抜いたもの)に接種し、30℃の温度で24時間、
静置させて培養する。培養液の濁度(波長660nmに
おける吸光度)が1.0以上に達していれば、その培養
液を以後の発酵に使用することができる。
[Preculture] The K-3 strain on the GYP agar medium was subjected to 5 to 100 mL of a GYP liquid medium using a platinum loop (the standard agar was removed from the GYP agar medium having the component composition shown in Table 1). Inoculate for 24 hours at a temperature of 30 ° C,
Let stand and culture. When the turbidity (absorbance at a wavelength of 660 nm) of the culture solution reaches 1.0 or more, the culture solution can be used for the subsequent fermentation.

【0033】〔γ―アミノ酪酸の測定方法〕試料を0.
2Nクエン酸ナトリウム緩衝液(pH2.2)で100
倍〜10,000倍に希釈した後、固形物を遠心分離ま
たは濾過により除去して、測定試料とした。γ―アミノ
酪酸およびグルタミン酸の各含有量は、アミノ酸含有量
の測定のための常法に従って高速液体クロマトグラフに
より以下の条件で測定した。 使用機器:(株)島津製作所製の高速液体クロマトグラ
フLC−9A 分析用カラム:強酸性陽イオン交換樹脂カラムShin
−pack Isc−07Na型 移動層緩衝液:(株)島津製作所製のアミノ酸移動層キ
ットNa型 移動層流量:0.3ml/分 反応層1:0.04%次亜塩素酸ナトリウム溶液(pH
10のホウ酸―炭酸緩衝液500mlに対して次亜塩素
酸0.2ml) 反応層2:(株)島津製作所製のアミノ酸分析キットO
PA試薬 反応層流量:0.2ml/分 検出:蛍光検出 Ex348nm、Em450nm
[Method for measuring γ-aminobutyric acid]
100 with 2N sodium citrate buffer (pH 2.2)
After diluting 1- to 10,000-fold, the solid matter was removed by centrifugation or filtration to obtain a measurement sample. The respective contents of γ-aminobutyric acid and glutamic acid were measured by a high performance liquid chromatograph under the following conditions according to a conventional method for measuring the amino acid content. Equipment used: High-performance liquid chromatograph LC-9A manufactured by Shimadzu Corporation Analytical column: Strongly acidic cation exchange resin column Shin
-Pack Isc-07 Na type moving layer buffer: amino acid moving layer kit manufactured by Shimadzu Corporation Na type moving layer flow rate: 0.3 ml / min Reaction layer 1: 0.04% sodium hypochlorite solution (pH
10 ml of boric acid-carbonic acid buffer solution to 0.2 ml of hypochlorous acid) Reaction layer 2: amino acid analysis kit O manufactured by Shimadzu Corporation
Flow rate of PA reagent reaction layer: 0.2 ml / min Detection: Fluorescence detection Ex348 nm, Em450 nm

【0034】[実施例1]100gのグルタミン酸ナト
リウムを含むGYP液体培地(表3に成分組成を示す)
1LにK−3株の前培養液1mLを添加し、30℃の温
度で培養した。培養液中のγ―アミノ酪酸の含有量は、
48時間後に48g/L、72時間後に51g/Lであ
った。また、グルタミン酸の含有量は、48時間後に8
g/L、72時間後に2g/Lであった。なお、100
gのグルタミン酸ナトリウム(一水和物)がγ−アミノ
酪酸に100%変換したときのγ―アミノ酪酸量は、約
55gであるため、γ―アミノ酪酸への変換率は、相対
的に、48時間後に87%、72時間後に93%である
と表すことができる。
Example 1 GYP liquid medium containing 100 g of sodium glutamate (Table 3 shows the composition of ingredients)
1 mL of the preculture liquid of the K-3 strain was added to 1 L, and the mixture was cultured at a temperature of 30 ° C. The content of γ-aminobutyric acid in the culture solution is
It was 48 g / L after 48 hours and 51 g / L after 72 hours. The content of glutamic acid is 8 after 48 hours.
g / L, 2 g / L after 72 hours. In addition, 100
Since the amount of γ-aminobutyric acid when 100 g of sodium glutamate (monohydrate) is 100% converted to γ-aminobutyric acid is about 55 g, the conversion rate to γ-aminobutyric acid is relatively 48%. It can be expressed as 87% after hours and 93% after 72 hours.

【0035】[0035]

【表3】 [Table 3]

【0036】[比較例]ワイン由来のラクトバチルス・
ヒルガルディーJCM1155株を使用し、それを実施
例1と同様の条件により培養した。この結果、得られた
培養液中のγ―アミノ酪酸の含有量は、48時間後およ
び72時間後共に0.05g/L以下であった。
Comparative Example Lactobacillus derived from wine
Hilgardee JCM1155 strain was used and cultured under the same conditions as in Example 1. As a result, the content of γ-aminobutyric acid in the obtained culture solution was 0.05 g / L or less after both 48 hours and 72 hours.

【0037】[実施例2]90℃の温度で10分間加熱
殺菌された発酵原料1(表4に成分組成を示す)50L
にK−3株の前培養液50mLを接種し、30℃の温度
で3日間培養した。発酵終了後の発酵液中のγ―アミノ
酪酸の含有量は、32g/Lであった。この発酵液を9
0℃の温度で10分間加熱殺菌し、それに活性炭を加え
て脱色処理し、珪藻土を含む濾過助剤を加えて濾過し、
真空濃縮機を用いて濃縮した後、噴霧乾燥機を用いて粉
末化させた。得られた粉末状食品中のγ―アミノ酪酸の
含有量は、16重量%であった。
[Example 2] 50 L of fermentation raw material 1 (the composition of which is shown in Table 4) sterilized by heating at a temperature of 90 ° C for 10 minutes
50 mL of the preculture liquid of the K-3 strain was inoculated into and was cultured at a temperature of 30 ° C. for 3 days. The content of γ-aminobutyric acid in the fermentation liquid after the fermentation was 32 g / L. 9 of this fermented liquid
Heat sterilize at a temperature of 0 ° C. for 10 minutes, add activated carbon to decolorize it, add a filter aid containing diatomaceous earth, and filter,
After concentrating with a vacuum concentrator, it was pulverized with a spray dryer. The content of γ-aminobutyric acid in the obtained powdered food was 16% by weight.

【0038】[0038]

【表4】 [Table 4]

【0039】[実施例3]90℃の温度で10分間加熱
殺菌された発酵調味液原料(表5に成分組成を示す)5
0LにK−3株の前培養液50mLを接種し、30℃の
温度で3日間培養した。発酵終了後の発酵液中のγ―ア
ミノ酪酸の含有量は、26g/Lであった。この発酵液
を90℃の温度で10分間加熱殺菌した後、真空濃縮機
を用いて濃縮した。得られた発酵調味液中のγ―アミノ
酪酸の含有量は、16重量%であった。
[Example 3] Fermented seasoning liquid raw material (component composition is shown in Table 5) 5 sterilized by heating at a temperature of 90 ° C for 10 minutes
50 mL of the preculture liquid of the K-3 strain was inoculated into 0 L and cultured at a temperature of 30 ° C. for 3 days. The content of γ-aminobutyric acid in the fermented liquid after the fermentation was 26 g / L. This fermented liquid was heat-sterilized at a temperature of 90 ° C. for 10 minutes and then concentrated using a vacuum concentrator. The content of γ-aminobutyric acid in the obtained fermented seasoning liquid was 16% by weight.

【0040】[0040]

【表5】 [Table 5]

【0041】さらに、得られた発酵調味液を、塩漬け白
菜を含むキムチ原料10kgに100mL加え、冷蔵庫
で1週間熟成させた。得られたキムチ中のγ―アミノ酪
酸の含有量は、100g当たり152mgであった。こ
の量は、添加したγ―アミノ酪酸の95%に相当する。
Further, 100 mL of the obtained fermented seasoning liquid was added to 10 kg of kimchi raw material containing salted Chinese cabbage and aged in a refrigerator for 1 week. The content of γ-aminobutyric acid in the obtained kimchi was 152 mg per 100 g. This amount corresponds to 95% of the added γ-aminobutyric acid.

【0042】[実施例4]90℃の温度で10分間加熱
殺菌された発酵原料2(表6に成分組成を示す)1,0
00LにK−3株の前培養液1Lを接種し、30℃の温
度で3日間培養した。発酵終了後の発酵液中のγ―アミ
ノ酪酸の含有量は、26g/Lであった。この発酵液を
90℃の温度で10分間加熱殺菌し、それに活性炭を加
えて脱色処理し、珪藻土を含む濾過助剤を加えて濾過
し、真空濃縮機を用いて濃縮した後、デキストリンを加
え噴霧乾燥機を用いて粉末化させた。得られた粉末状食
品中のγ―アミノ酪酸の含有量は、30重量%であっ
た。真空濃縮機を用いて濃縮した。得られた発酵調味液
中のγ―アミノ酪酸の含有量は、16重量%であった。
[Example 4] Fermentation raw material 2 heat-sterilized at a temperature of 90 ° C for 10 minutes (the composition of ingredients is shown in Table 6) 1,0
00 L was inoculated with 1 L of the preculture liquid of the K-3 strain and cultured at a temperature of 30 ° C. for 3 days. The content of γ-aminobutyric acid in the fermented liquid after the fermentation was 26 g / L. This fermented liquid is sterilized by heating at 90 ° C for 10 minutes, decolorized by adding activated carbon to it, filtered by adding a filter aid containing diatomaceous earth, concentrated by using a vacuum concentrator, and then sprayed with dextrin. It was pulverized using a dryer. The content of γ-aminobutyric acid in the obtained powdered food was 30% by weight. It concentrated using the vacuum concentrator. The content of γ-aminobutyric acid in the obtained fermented seasoning liquid was 16% by weight.

【0043】[0043]

【表6】 [Table 6]

【0044】[実施例5]90℃の温度で10分間加熱
殺菌された発酵原料3(表7に成分組成を示す)100
LにK−3株の前培養液100mLを接種し、30℃の
温度で24時間培養した後、pHを5.0に再調整し、
さらに2日間培養を続けた。発酵終了後の発酵液中のγ
―アミノ酪酸の含有量は、54g/Lであった。この発
酵液を90℃の温度で10分間加熱殺菌し、珪藻土を含
む濾過助剤を加えて濾過し、真空濃縮機を用いて濃縮し
た後、凍結乾燥機を用いて粉末化させた。得られた粉末
状食品中のγ―アミノ酪酸の含有量は、70重量%であ
った。
[Example 5] 100 of fermentation raw material 3 (the composition of which is shown in Table 7) sterilized by heating at 90 ° C for 10 minutes
L was inoculated with 100 mL of the preculture liquid of the K-3 strain, cultivated at a temperature of 30 ° C. for 24 hours, and then the pH was readjusted to 5.0,
The culture was continued for another 2 days. Γ in fermented liquid after fermentation
-The content of aminobutyric acid was 54 g / L. This fermented liquid was sterilized by heating at a temperature of 90 ° C. for 10 minutes, filtered by adding a filter aid containing diatomaceous earth, concentrated using a vacuum concentrator, and then pulverized using a freeze dryer. The content of γ-aminobutyric acid in the obtained powdered food was 70% by weight.

【0045】[0045]

【表7】 [Table 7]

【0046】[0046]

【発明の効果】請求項1に係る発明のγ−アミノ酪酸生
産能を有する乳酸菌を使用すると、グルタミン酸または
その塩類を高濃度に含有する発酵原料を発酵処理して、
γ−アミノ酪酸を高い割合で含有する食品を得ることが
できる。
When the lactic acid bacterium capable of producing γ-aminobutyric acid of the invention according to claim 1 is used, a fermentation raw material containing glutamic acid or a salt thereof at a high concentration is subjected to fermentation treatment,
A food containing a high proportion of γ-aminobutyric acid can be obtained.

【0047】請求項2に係る発明の乳酸菌では、請求項
1に係る発明による上記効果が確実に得られる。
With the lactic acid bacterium of the invention according to claim 2, the above-mentioned effect according to the invention of claim 1 can be reliably obtained.

【0048】請求項3に係る発明の製造方法によると、
γ−アミノ酪酸を高い割合で含有する食品を製造するこ
とができる。
According to the manufacturing method of the invention of claim 3,
Foods containing a high proportion of γ-aminobutyric acid can be produced.

【0049】請求項4に係る発明の製造方法では、乳酸
菌の増殖が最も促進され、γ−アミノ酪酸を生産する能
力が向上するので、より効率良く、γ−アミノ酪酸を高
い割合で含有する食品が得られる。
In the production method of the invention according to claim 4, since the growth of lactic acid bacteria is most promoted and the ability to produce γ-aminobutyric acid is improved, the food containing γ-aminobutyric acid in a high proportion is more efficient. Is obtained.

【0050】請求項5に係る発明の製造方法では、γ−
アミノ酪酸を高い割合で含有する粉末状の食品が得られ
る。
In the manufacturing method of the invention according to claim 5, γ-
A powdery food product containing a high proportion of aminobutyric acid is obtained.

【0051】請求項6に係る発明の製造方法では、発酵
液の濃縮液が添加されて、γ−アミノ酪酸を高い割合で
含有する飲食物が得られる。
In the production method according to the sixth aspect of the present invention, the concentrated liquid of the fermentation broth is added to obtain a food or drink containing a high proportion of γ-aminobutyric acid.

【0052】請求項7に係る発明の製造方法では、γ−
アミノ酪酸を高い割合で含有する粉末が添加されて、γ
−アミノ酪酸を高い割合で含有する飲食物が得られる。
In the manufacturing method of the invention according to claim 7, γ-
A powder containing a high proportion of aminobutyric acid was added to give γ
-Foods and drinks containing a high proportion of aminobutyric acid are obtained.

フロントページの続き (72)発明者 上野 義栄 京都市右京区太秦安井車道町21−27セント ポーリア太秦II102号 (72)発明者 東口 伸二 京都市南区吉祥院石原堂の後西町24番5号 株式会社ファーマフーズ研究所内 (72)発明者 金 武祚 京都市南区吉祥院石原堂の後西町24番5号 株式会社ファーマフーズ研究所内 Fターム(参考) 4B018 LB01 LB03 LB08 MD19 MD86 ME04 ME14 MF13 4B065 AA30X BA21 BB02 BB03 BB12 BB15 BB29 CA17 CA41Continued front page    (72) Inventor Yoshie Ueno             21-27 cents, Uzumasa Yasui Road Road, Ukyo-ku, Kyoto             Paulia Uzumasa II 102 (72) Inventor Shinji Higashiguchi             24-5 Gonishimachi, Kichijoin Ishiharado, Minami-ku, Kyoto-shi               Pharma Foods Co., Ltd. (72) Inventor Kim Takehisa             24-5 Gonishimachi, Kichijoin Ishiharado, Minami-ku, Kyoto-shi               Pharma Foods Co., Ltd. F term (reference) 4B018 LB01 LB03 LB08 MD19 MD86                       ME04 ME14 MF13                 4B065 AA30X BA21 BB02 BB03                       BB12 BB15 BB29 CA17 CA41

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 キムチから単離された菌株であって、培
地にグルタミン酸またはその塩類を添加することにより
増殖が促進されてグルタミン酸脱炭酸酵素の作用により
γ―アミノ酪酸を生成するラクトバチルス・ヒルガルデ
ィーに属する、γ―アミノ酪酸生産能を有する乳酸菌。
1. A strain isolated from kimchi, the growth of which is promoted by the addition of glutamic acid or a salt thereof to the medium, and Lactobacillus hirgardii that produces γ-aminobutyric acid by the action of glutamate decarboxylase. A lactic acid bacterium having the ability to produce γ-aminobutyric acid.
【請求項2】 前記菌株がラクトバチルス・ヒルガルデ
ィーK−3株 FERM P−18422である請求項
1記載の、γ―アミノ酪酸生産能を有する乳酸菌。
2. The lactic acid bacterium capable of producing γ-aminobutyric acid according to claim 1, wherein the strain is Lactobacillus hilgardi K-3 strain FERM P-18422.
【請求項3】 グルタミン酸またはその塩類を含有する
発酵原料に、請求項1または請求項2記載の乳酸菌を接
種し培養して、γ−アミノ酪酸を含有する発酵物を得る
ことを特徴とする食品の製造方法。
3. A food product, characterized in that a fermentation raw material containing glutamic acid or a salt thereof is inoculated with the lactic acid bacterium according to claim 1 or 2 and cultured to obtain a fermented product containing γ-aminobutyric acid. Manufacturing method.
【請求項4】 初発pH4.5〜5.5で発酵処理を行
う、請求項3記載の食品の製造方法。
4. The method for producing a food according to claim 3, wherein the fermentation treatment is performed at an initial pH of 4.5 to 5.5.
【請求項5】 前記発酵物が発酵液であり、その発酵液
を濾過、濃縮および乾燥させて、γ−アミノ酪酸を含有
する粉末を得る、請求項3または請求項4記載の食品の
製造方法。
5. The method for producing a food product according to claim 3, wherein the fermented product is a fermented liquid, and the fermented liquid is filtered, concentrated and dried to obtain a powder containing γ-aminobutyric acid. .
【請求項6】 前記発酵物が発酵液であり、その発酵液
を濃縮した後に食物または飲料に添加して、γ−アミノ
酪酸を含有する飲食物を得る、請求項3または請求項4
記載の食品の製造方法。
6. The fermented product is a fermented liquor, and the fermented liquor is concentrated and then added to food or beverage to obtain a food or drink containing γ-aminobutyric acid.
A method for producing the described food.
【請求項7】 前記粉末を食物または飲料に添加して、
γ−アミノ酪酸を含有する飲食物を得る、請求項5記載
の食品の製造方法。
7. Adding the powder to a food or beverage,
The method for producing a food according to claim 5, wherein a food or drink containing γ-aminobutyric acid is obtained.
JP2001268696A 2001-09-05 2001-09-05 Method for producing foods using lactic acid bacteria capable of producing γ-aminobutyric acid Expired - Lifetime JP3880820B2 (en)

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* Cited by examiner, † Cited by third party
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JP2003088335A (en) * 2001-09-14 2003-03-25 Pharmafoods Kenkyusho:Kk Food composition for improving urination function, and good and drink containing the same
JP2005065691A (en) * 2003-08-06 2005-03-17 Akita Prefecture COMPOSITION CONTAINING gamma-AMINOBUTYRIC ACID AND METHOD FOR MANUFACTURING THE SAME
JP2005198578A (en) * 2004-01-16 2005-07-28 Ehime Prefecture METHOD FOR PRODUCING gamma-AMINOBUTYRIC ACID AND FERMENTED LIQUID YIELDED THEREBY
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JP2006061088A (en) * 2004-08-27 2006-03-09 Pharma Foods International Co Ltd Concentration power-improving drink or food
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JP2008017785A (en) * 2006-07-14 2008-01-31 Mikasa Sangyo Kk METHOD FOR ENRICHING COMMON SALT-CONTAINING FOOD WITH gamma-AMINOBUTYRIC ACID
JP4815493B2 (en) * 2005-12-27 2011-11-16 シージェイ チェイルジェダン コープ. Medium composition containing fermented gochujang, brewed soy sauce stock or acid-decomposed soy sauce stock, and method for producing γ-aminobutyric acid
KR20220048748A (en) * 2020-10-13 2022-04-20 전남대학교산학협력단 Lactobacillus hilgardii STRAIN FOR PRODUCING GABA AND METHOD FOR PRODUCING USING THE SAME
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003088335A (en) * 2001-09-14 2003-03-25 Pharmafoods Kenkyusho:Kk Food composition for improving urination function, and good and drink containing the same
JP2005065691A (en) * 2003-08-06 2005-03-17 Akita Prefecture COMPOSITION CONTAINING gamma-AMINOBUTYRIC ACID AND METHOD FOR MANUFACTURING THE SAME
JP2005198578A (en) * 2004-01-16 2005-07-28 Ehime Prefecture METHOD FOR PRODUCING gamma-AMINOBUTYRIC ACID AND FERMENTED LIQUID YIELDED THEREBY
JP2005312438A (en) * 2004-03-29 2005-11-10 Marukome Kk FOOD MATERIAL WITH HIGH gamma-AMINOBUTYRIC ACID CONTENT AND METHOD FOR PRODUCING THE SAME
JP2006061088A (en) * 2004-08-27 2006-03-09 Pharma Foods International Co Ltd Concentration power-improving drink or food
KR100740867B1 (en) 2005-04-29 2007-07-19 (주)바이오벤 Media for Culturing Lactic Acid Bacteria Used for Preparing High Concentrated ????
JP4815493B2 (en) * 2005-12-27 2011-11-16 シージェイ チェイルジェダン コープ. Medium composition containing fermented gochujang, brewed soy sauce stock or acid-decomposed soy sauce stock, and method for producing γ-aminobutyric acid
JP2008017785A (en) * 2006-07-14 2008-01-31 Mikasa Sangyo Kk METHOD FOR ENRICHING COMMON SALT-CONTAINING FOOD WITH gamma-AMINOBUTYRIC ACID
KR20220048748A (en) * 2020-10-13 2022-04-20 전남대학교산학협력단 Lactobacillus hilgardii STRAIN FOR PRODUCING GABA AND METHOD FOR PRODUCING USING THE SAME
KR102438706B1 (en) * 2020-10-13 2022-08-31 전남대학교산학협력단 Lactobacillus hilgardii STRAIN FOR PRODUCING GABA AND METHOD FOR PRODUCING USING THE SAME
CN116286513A (en) * 2023-02-27 2023-06-23 山东福瑞达生物科技有限公司 Lactobacillus johnsonii FR-1012 and method for industrially producing gamma-aminobutyric acid by same
CN116286513B (en) * 2023-02-27 2024-01-23 山东福瑞达生物科技有限公司 Lactobacillus johnsonii FR-1012 and method for industrially producing gamma-aminobutyric acid by same

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