JP2001112437A - Production of food and drink containing bacteria of genus bifidobacterium - Google Patents

Production of food and drink containing bacteria of genus bifidobacterium

Info

Publication number
JP2001112437A
JP2001112437A JP29530099A JP29530099A JP2001112437A JP 2001112437 A JP2001112437 A JP 2001112437A JP 29530099 A JP29530099 A JP 29530099A JP 29530099 A JP29530099 A JP 29530099A JP 2001112437 A JP2001112437 A JP 2001112437A
Authority
JP
Japan
Prior art keywords
culture
bifidobacterium
bacteria
culture solution
solution
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.)
Pending
Application number
JP29530099A
Other languages
Japanese (ja)
Inventor
Hirokazu Tsuji
浩和 辻
Yasuhisa Shimakawa
康久 島川
Mika Miura
みか 三浦
Haruo Ikemura
治夫 池邨
Takashi Morishita
▼隆▲ 森下
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.)
Yakult Honsha Co Ltd
Original Assignee
Yakult Honsha 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 Yakult Honsha Co Ltd filed Critical Yakult Honsha Co Ltd
Priority to JP29530099A priority Critical patent/JP2001112437A/en
Publication of JP2001112437A publication Critical patent/JP2001112437A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a process for the economical production of a food or drink such as fermented milk and yogurt containing bacteria of the genus Bifidobacterium and having high survival ratio of the bacteria in the product. SOLUTION: The objective process for the production of a food or drink containing bacteria of the genus Bifidobacterium is characterized by the introduction of a step to decrease the proliferation speed of the bacteria during the cultivation of the bacteria without stopping the metabolism of the bacteria.

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】本発明は、優れた生理活性を
有するビフィドバクテリウム属細菌の生残性が改善され
た飲食品の製造方法及びこの方法により得られるビフィ
ドバクテリウム属細菌含有飲食品に関するものである。
[0001] The present invention relates to a method for producing a food or drink having improved survival of a Bifidobacterium bacterium having excellent physiological activity, and a food and drink containing a Bifidobacterium bacterium obtained by this method. It is about goods.

【0002】[0002]

【従来の技術】ビフィドバクテリウム属細菌は人の大腸
に多く成育し、整腸効果や病原菌の抑制効果が認められ
ている細菌である。このため、発酵乳や固形ヨーグルト
など多くの飲食物に利用されている。
2. Description of the Related Art Bifidobacterium bacteria grow in the large intestine of humans, and have been shown to have an intestinal regulation effect and an inhibitory effect on pathogenic bacteria. For this reason, it is used in many foods and drinks such as fermented milk and solid yogurt.

【0003】しかしながら、ビフィドバクテリウム属細
菌は一般的に酸素や低pHに弱いので、製品化後の生菌数
を維持することが困難である。例えばビフィドバクテリ
ウム属細菌を含有する飲食物を通気性の容器に充填する
と、酸素の影響を受け、製品保存時にその菌数が減少し
てしまう。また、発酵乳のような低pH域の製品中ではビ
フィドバクテリウム属細菌の菌数が、保存中に減少して
しまうという問題がある。更に製品化する際、シロップ
等を加えるため、浸透圧による菌数の減少及び温度によ
る菌数の減少という問題もある。このように発酵乳等に
製品化した後に菌数が減少してしまうと、発酵乳等のビ
フィドバクテリウム属細菌の生理作用が減退することに
なる。このため、製品保存時の菌数維持が重要な課題と
なっており、通常はアルミを蒸着した紙パックや、ガラ
ス容器等を容器素材として使用し、容器内を嫌気状態に
保つ試み等がなされている。しかし容器の充填時の酸素
の影響はまぬがれない。
[0003] However, Bifidobacterium bacteria are generally susceptible to oxygen and low pH, so it is difficult to maintain the viable cell count after commercialization. For example, when a food or drink containing a Bifidobacterium bacterium is filled in a gas-permeable container, the number of bacteria is reduced during storage of the product due to the influence of oxygen. Further, there is a problem that the number of bacteria of the genus Bifidobacterium decreases in a product having a low pH range such as fermented milk during storage. Furthermore, since syrup and the like are added at the time of commercialization, there is a problem that the number of bacteria decreases due to osmotic pressure and the number of bacteria decreases due to temperature. If the number of bacteria decreases after commercialization into fermented milk or the like, the physiological action of Bifidobacterium bacteria such as fermented milk will be reduced. For this reason, maintaining the number of bacteria during storage of the product has become an important issue.In general, attempts have been made to use a paper pack or a glass container on which aluminum is deposited as a container material and keep the inside of the container in an anaerobic state. ing. However, the effect of oxygen during filling of the container is inevitable.

【0004】また、一方ではビフィドバクテリウム属細
菌の生残性を改善する方法が提案されている。例えば、
特公昭57−4291号公報にはソルビトールを発酵乳
1Lあたり0.2〜1.0モル添加するビフィドバクテ
リウム属細菌の生残性改善方法が開示されている。ま
た、特開平6−253734号公報にはエリスリトール
を生残性改善剤として添加する方法が開示されている。
[0004] On the other hand, a method for improving the survival of Bifidobacterium bacteria has been proposed. For example,
Japanese Patent Publication No. 57-4291 discloses a method for improving the viability of a bacterium belonging to the genus Bifidobacterium, in which sorbitol is added in an amount of 0.2 to 1.0 mol per liter of fermented milk. Japanese Patent Application Laid-Open No. 6-253,734 discloses a method of adding erythritol as a survival improver.

【0005】しかしながら、このようなビフィドバクテ
リウム属細菌の生残性改善剤の添加は、製造コストの上
昇を招くうえに、その生残性改善効果には改善の余地が
残っており、より実用性の高い生残性改善策の提供が求
められている。
[0005] However, the addition of the agent for improving the survival of Bifidobacterium genus causes an increase in the production cost, and there is still room for improvement in the effect of improving the survival. There is a need to provide highly viable survival improvement measures.

【0006】更に、近年では、自然な風味が嗜好される
傾向が強く、添加剤等を使用しないで生残性を改善する
製造法が要求されている。
Furthermore, in recent years, natural flavors have a strong tendency to be tasted, and there is a demand for a production method that improves the survival without using additives and the like.

【0007】[0007]

【発明が解決しようとする課題】従って、本発明の目的
は、発酵乳やヨーグルト等の製品中での生残率が高いビ
フィドバクテリウム属細菌含有飲食品の経済的な製造法
を提供することにある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a method for economically producing a food or drink containing Bifidobacterium bacteria having a high survival rate in products such as fermented milk and yogurt. It is in.

【0008】[0008]

【課題を解決するための手段】斯かる実状に鑑み本発明
者は鋭意研究を行った結果、ビフィドバクテリウム属細
菌の培養途中、該細菌の代謝を停止させずに増殖速度を
低下させる工程を加えれば、その後の生残率が高い細菌
含有飲食品が得られることを見出し本発明を完成した。
Means for Solving the Problems In view of such a situation, the present inventors have conducted intensive studies and as a result, during the culture of Bifidobacterium bacteria, a step of reducing the growth rate without stopping the metabolism of the bacteria. And found that a bacterial food or drink having a high survival rate can be obtained thereafter, and completed the present invention.

【0009】すなわち、本発明は、ビフィドバクテリウ
ム属細菌の培養途中に、該細菌の代謝を停止させずに増
殖速度を低下させる工程を導入することを特徴とするビ
フィドバクテリウム属細菌含有飲食品の製造方法及びこ
の製造方法により得られた該細菌を含有する飲食品を提
供するものである。
That is, the present invention provides a method for producing a bacterium of the genus Bifidobacterium, which comprises introducing a step of reducing the growth rate without stopping metabolism of the bacterium of the genus Bifidobacterium during the cultivation of the bacterium of the genus Bifidobacterium. It is intended to provide a method for producing food and drink and a food and drink containing the bacterium obtained by the production method.

【0010】[0010]

【発明の実施の形態】本発明において、ビフィドバクテ
リウム属細菌の代謝を停止させずに増殖速度を低下させ
る工程とは、ビフィドバクテリウム属細菌培養時の最適
条件が定まっている各種の環境要因、すなわち、浸透
圧、培地pH、溶存酸素濃度、培養温度等を、菌の代謝を
止めない範囲内で、通常の培養条件から変化させる工程
のことである。通常、これらの環境要因を悪化させると
ビフィドバクテリウム属細菌が傷害を受け、その死滅が
促進されるものと考えられているため、それらを故意に
与える工程がビフィドバクテリウム属細菌含有飲食品の
製造時に適用されることはなかった。因に通常の培養条
件は菌種によって異なるが、一般的には浸透圧150〜
900mOsm(ミリオズモ)、pH4.0〜7.0、溶存酸
素濃度0〜2ppm、培養温度30〜39℃程度である。
DETAILED DESCRIPTION OF THE INVENTION In the present invention, the step of reducing the growth rate without stopping the metabolism of Bifidobacterium bacterium refers to various kinds of methods in which the optimal conditions for culturing Bifidobacterium bacterium are determined. This is a step of changing environmental factors, that is, osmotic pressure, medium pH, dissolved oxygen concentration, culture temperature, and the like, from normal culture conditions within a range that does not stop bacterial metabolism. It is generally thought that exacerbating these environmental factors may damage Bifidobacterium bacteria and promote their death, so the step of intentionally providing them is a diet containing Bifidobacterium bacteria. It was not applied during the manufacture of the product. The usual culturing conditions vary depending on the bacterial species, but generally, the osmotic pressure is 150 to
900 mOsm (milliosmo), pH 4.0 to 7.0, dissolved oxygen concentration 0 to 2 ppm, culture temperature 30 to 39 ° C.

【0011】しかしながら、このような工程を培養途中
に導入することにより、ビフィドバクテリウム属細菌の
生残性が改善され、特にこれを含有する飲食品中での生
残性がよいことを本発明者は見出した。
However, by introducing such a step during the cultivation, the survival of Bifidobacterium bacterium is improved, and particularly, it is shown that the survival of foods and beverages containing the same is good. The inventor has found.

【0012】ビフィドバクテリウム属細菌の代謝を停止
させずに増殖速度を低下させる工程としては、次のもの
が挙げられる。 (a)培養液中の溶存酸素量を増加させる工程 (b)培養液の温度を変化させる工程 (c)培養液の浸透圧を変化させる工程 (d)培養液のpHを変化させる工程 これらは、いずれか1つでも、2以上の組みあわせであ
ってもよい。なお、その他の工程としては、胆汁溶液等
界面活性作用を有する物質を添加する工程等が挙げられ
る。
The steps for reducing the growth rate without stopping the metabolism of Bifidobacterium bacteria include the following. (A) Step of increasing the amount of dissolved oxygen in the culture solution (b) Step of changing the temperature of the culture solution (c) Step of changing the osmotic pressure of the culture solution (d) Step of changing the pH of the culture solution , Or a combination of two or more. In addition, as another step, a step of adding a substance having a surface active effect such as a bile solution and the like can be mentioned.

【0013】上記工程の適用時期は制限されず、ビフィ
ドバクテリウム属細菌致達菌数と培養時間を考慮して決
定すればよいが、培養の後期、一般にビフィドバクテリ
ウム属細菌の菌体濃度が1×107cfu/ml〜1.5×1
9cfu/ml、特に7×107cfu/ml〜1.5×109cfu
/ml程度となる時期に適用することが好ましい。変化さ
せた環境要因を元に戻すことは困難であるため、菌数が
1×107cfu/ml程度以下の段階で該工程を適用する
と、その後の増殖に時間がかかってしまうか、pHや温度
等を元に戻すための余分な添加物、工程までも必要とな
ってしまい、1.5×109cfu/ml以上まで培養してし
まうと、菌の活性が低下してしまうためである。また、
上記範囲であれば、培養の前半もしくは中盤において該
工程を適用させるよりも、好適な生残性を得られるので
ある。
The application time of the above step is not limited, and may be determined in consideration of the number of bacteria reached by the genus Bifidobacterium and the culturing time. The concentration is 1 × 10 7 cfu / ml to 1.5 × 1
09 cfu / ml, especially 7 × 10 7 cfu / ml to 1.5 × 10 9 cfu
/ Ml is preferably applied at a time when it becomes about / ml. Since it is difficult to restore the changed environmental factors, if this step is applied at a stage where the number of bacteria is about 1 × 10 7 cfu / ml or less, it will take time for subsequent growth, This is because extra additives and steps for restoring the temperature and the like are required, and if the culture is carried out to 1.5 × 10 9 cfu / ml or more, the activity of the bacteria is reduced. . Also,
Within the above range, a more favorable survivability can be obtained than when the step is applied in the first half or the middle of the culture.

【0014】更に、該工程の作用時間は、1時間以上と
することが好ましく、2時間以上行うことがより好まし
い。該工程の適用時には与えられた環境変化に対応する
ためのタンパク質等が誘導されていると考えられ、この
誘導タンパク質が生残性改善に何らかの形で寄与してい
ると考えられるため、充分な誘導を達成するには上記の
作用時間を取ることが望ましいのである。ここで、菌の
代謝を止めないために、上記の工程は温度30℃〜42
℃の範囲内で行う必要がある。すなわち、従来の発酵乳
等ビフィドバクテリウム属細菌含有飲食品製造工程で行
われていた、培養液の冷却した後のシロップ液との調
合、酸の添加等では、浸透圧差、pH差による環境変化が
起きても、代謝が停止又は非常に延滞しているため、タ
ンパク質等が充分に誘導されず、優れた生残性は得られ
ないのである。本発明における菌の代謝を停止させずに
増殖速度を低下させる工程をより詳細に説明する。
Further, the operation time of the step is preferably at least 1 hour, more preferably at least 2 hours. At the time of applying this step, it is considered that a protein or the like for responding to a given environmental change is induced, and it is considered that this induced protein contributes in some way to the improvement of viability. In order to achieve the above, it is desirable to take the above action time. Here, in order not to stop the metabolism of the bacterium, the above-mentioned process is performed at a temperature of 30 ° C.
It must be performed within the range of ° C. That is, in the conventional manufacturing process of food or beverage containing Bifidobacterium bacterium such as fermented milk, the preparation of a culture solution with a syrup solution after cooling, the addition of an acid, etc., are caused by the difference in osmotic pressure and pH. Even if a change occurs, metabolism is stopped or extremely delayed, so that proteins and the like are not sufficiently induced, and excellent survivability cannot be obtained. The step of reducing the growth rate without stopping the metabolism of bacteria in the present invention will be described in more detail.

【0015】(a)培養液中の溶存酸素量を増加させる
工程 培養液中の溶存酸素を増加させる工程としては、培養槽
(発酵槽)の攪拌工程;振盪工程;発酵槽内雰囲気の酸
素置換工程;無機物、微生物、酸素等の酸素発生(剤)
を添加する工程等が挙げられる。これらの酸素供給手段
等は、培養途中の溶存酸素量を増加させるものであれば
いずれも用いることができ、特に培養終点の4時間程度
前から2〜4時間程度の処理を行えば、高い生残性改善
効果を得ることが可能である。このとき、培養槽中の溶
存酸素濃度は2ppm〜培地中の飽和酸素濃度、特に3ppm
〜培地中の飽和酸素濃度の範囲に維持することが好ま
しい。2ppm 未満では十分な生残性改善効果が得られな
いためである。
(A) Step of increasing the amount of dissolved oxygen in the culture solution The step of increasing the amount of dissolved oxygen in the culture solution includes a step of stirring the culture tank (fermenter); a shaking step; Process: generation of oxygen such as inorganic substances, microorganisms, and oxygen (agent)
And the like. Any of these oxygen supply means can be used as long as they increase the amount of dissolved oxygen during cultivation. Particularly, if the treatment is performed for about 2 to 4 hours from about 4 hours before the end point of cultivation, high productivity can be obtained. It is possible to obtain a residual improvement effect. At this time, the dissolved oxygen concentration in the culture tank is 2 ppm to the saturated oxygen concentration in the medium, especially 3 ppm.
It is preferable to maintain the concentration within the range of the saturated oxygen concentration in the medium. If the amount is less than 2 ppm, a sufficient survival improving effect cannot be obtained.

【0016】(b)培養液の温度を変化させる工程 培養温度を変化させる工程としては、培養槽への温水又
は冷水循環工程;高温に保持された水、乳培地、微生物
の培養液又はシロップ液等を添加する工程、発熱剤の添
加工程等が挙げられる。この場合にも、培養終点の4時
間程度前から2〜4時間程度の処理を行えば、高い生残
性改善効果を得ることが可能であり、その培養温度は元
の培養条件(例えば、ビフィドバクテリウム・ブレー
ベ、ビフィドバクテリウム・ビフィダムであれば30〜
39℃)から3〜12℃変化させることが好ましく、特
に6〜12℃程度変化させた後維持することが好まし
い。3℃未満の変化では、生残性改善効果がやや不十分
な場合もあり、14℃以上では菌が死滅してしまう場合
もあるためである。なお、温度変化としては、温度を上
昇させることがより好ましいが、ビフィドバクテリウム
属細菌の死滅を防ぐためには、42℃以下とすることが
望ましい。
(B) Step of changing the temperature of the culture solution The step of changing the culture temperature includes the step of circulating hot or cold water to the culture tank; water, a milk medium, and a culture or syrup of microorganisms maintained at a high temperature. And the step of adding a heating agent. Also in this case, if the treatment is carried out for about 2 to 4 hours from about 4 hours before the end point of the culture, it is possible to obtain a high viability improving effect, and the culture temperature is adjusted to the original culture conditions (for example, 30 for Fidobacterium breve and Bifidobacterium bifidum
(39 ° C.), preferably from 3 to 12 ° C., more preferably from 6 to 12 ° C. If the change is less than 3 ° C., the effect of improving survival may be slightly insufficient, and if it is 14 ° C. or more, the bacteria may be killed. It is more preferable to increase the temperature as the temperature change, but it is preferable to set the temperature to 42 ° C. or lower in order to prevent the death of Bifidobacterium bacteria.

【0017】(c)培養液の浸透圧を変化させる工程 培養液の浸透圧を変化させる工程としては、培養途中で
培養液よりも浸透圧の高いシロップ液等を培養液に混合
する工程;異なる濃度の乳成分を培養液に混合する工
程;温水の混合工程;無機又は有機酸の混合工程等が挙
げられる。この場合、変化させる浸透圧差は元の浸透圧
によりやや異なるが、通常元の培養条件(例えば、通常
の培地となる20%程度の乳培地では600mOsm程度)
から150〜800mOsm変化させることが好ましく、特
に200〜400mOsm程度変化させた後2時間以上維持
することが好ましい。150mOsm未満の変化では、生残
性改善効果がやや不十分な場合もあり、400mOsm以上
では菌が死滅してしまう場合もあるためである。また、
変化させた浸透圧を元に戻すことは、飲食品の製造工程
上困難な場合が多いため、該工程は培養終点に合わせ適
宜適用することが好ましい。なお、浸透圧変化として
は、浸透圧を上昇させることがより好ましいが、(b)
と同様の理由から最終製品の(又は工程の適用後の)最
終浸透圧を1000mOsm以下とすることが望ましい。
(C) Step of changing the osmotic pressure of the culture medium The step of changing the osmotic pressure of the culture medium includes mixing a syrup having a higher osmotic pressure than the culture medium into the culture medium during the culturing; A step of mixing a milk component having a concentration with a culture solution; a step of mixing warm water; a step of mixing an inorganic or organic acid. In this case, the osmotic pressure difference to be changed is slightly different depending on the original osmotic pressure, but usually under the original culture conditions (for example, about 600 mOsm in a 20% milk medium which is a normal medium).
It is preferable that the temperature is changed from about 150 to 800 mOsm, and it is particularly preferable that the temperature is changed for about 200 to 400 mOsm and then maintained for 2 hours or more. If the change is less than 150 mOsm, the effect of improving survival may be somewhat insufficient, and if it is 400 mOsm or more, the bacteria may be killed. Also,
Since it is often difficult to restore the changed osmotic pressure to the original in the production process of foods and drinks, it is preferable to appropriately apply this process according to the end point of the culture. As the change in osmotic pressure, it is more preferable to increase the osmotic pressure.
For the same reason as described above, it is desirable that the final osmotic pressure of the final product (or after application of the process) is 1000 mOsm or less.

【0018】(d)培養液のpHを変化させる工程 培養液のpHを変化させる工程としては、培養液中への培
養液への酸添加工程;異なるpHの培養液やシロップ液と
の混合工程等が挙げられる。この場合にも、培養終点の
4時間程度前から2〜4時間程度の処理を行えば、高い
生残性改善効果を得ることが可能であり、そのpH変化の
度合いは元の培養条件から0.3〜3.0変化させるこ
とが好ましく、特に0.5〜1.5程度変化させた後維
持することが好ましい。0.3未満の変化では、生残性
改善効果がやや不十分な場合もあり、3.0以上では菌
が死滅してしまう場合もあるためである。なお、pH変化
としては、pHを低下させることがより好ましく、上記と
同様に製品の(又は工程の適用後の)最終pHを4〜5.
5以下とすることが望ましい。また、酸添加で使用する
酸は、クエン酸、リンゴ酸、乳酸、コハク酸、アスコル
ビン酸、酢酸、ピルビン酸等の有機酸、塩酸、硫酸等の
無機酸等いずれでもよく風味面からクエン酸、リンゴ
酸、乳酸が特に好ましい。
(D) Step of changing the pH of the culture solution The step of changing the pH of the culture solution includes a step of adding an acid to the culture solution into the culture solution; and a process of mixing the culture solution or syrup solution with different pH. And the like. Also in this case, if the treatment is performed for about 2 to 4 hours from about 4 hours before the end point of the culture, a high survival improving effect can be obtained, and the degree of the pH change is 0% from the original culture conditions. It is preferable to change the value by about 0.3 to 3.0, and it is particularly preferable to maintain the value after changing about 0.5 to 1.5. If the change is less than 0.3, the effect of improving survival may be slightly insufficient, and if it is 3.0 or more, the bacteria may be killed. As the pH change, it is more preferable to lower the pH, and the final pH of the product (or after application of the step) is 4 to 5.
It is desirably 5 or less. Further, the acid used in the acid addition may be citric acid, malic acid, lactic acid, succinic acid, ascorbic acid, acetic acid, organic acids such as pyruvic acid, hydrochloric acid, inorganic acids such as sulfuric acid, etc. Malic acid and lactic acid are particularly preferred.

【0019】上記工程は、いずれも容易に製造工程に導
入できるものであり、これをそのままあるいは任意の他
の方法と組み合わせることにより生残性を改善すること
ができる。これらの工程は1種又は2種以上を組み合わ
せて使用してもよい。
Any of the above steps can be easily introduced into the manufacturing process, and the survival can be improved by using it as it is or by combining it with any other method. These steps may be used alone or in combination of two or more.

【0020】一方、上記因子を与える工程以外の培養工
程は、通常の培養条件を用いればよい。例えば、スター
ター接種時の菌体濃度は0.05から5%程度、培養液
の酸素濃度は通常0〜2ppm(25℃)、浸透圧は15
0〜900mOsm、初発pHは7.5〜5.5として培養を
行えばよい。また、培養温度はビフィドバクテリウム属
細菌各々の至適温度にあわせおよそ30℃〜39℃とし
て培養を行えばよい。その際に様々な培地成分を適宜添
加してもよい。
On the other hand, in the culture steps other than the step of providing the above factors, ordinary culture conditions may be used. For example, the cell concentration at the starter inoculation is about 0.05 to 5%, the oxygen concentration of the culture is usually 0 to 2 ppm (25 ° C.), and the osmotic pressure is 15
Culture may be performed at 0 to 900 mOsm and the initial pH is 7.5 to 5.5. The cultivation temperature may be about 30 ° C. to 39 ° C. in accordance with the optimal temperature of each of the bacteria belonging to the genus Bifidobacterium. At that time, various medium components may be appropriately added.

【0021】本発明の方法に用いることの可能なビフィ
ドバクテリウム属細菌の種類は特に限定されるものでは
なく、例えば、ビフィドバクテリウム・ブレーベ(Bifi
dobacterium breve)、ビフィドバクテリウム・ロンガ
ム(Bifidobacterium longum)、ビフィドバクテリウム
・ビフィダム(Bifidobacterium bifidum)、ビフィド
バクテリウム・アニマーリス(Bifidobacterium animal
is)、ビフィドバクテリウム・ズイス(Bifidobacteriu
m suis)、ビフィドバクテリウム・インファンティス
Bifidobacterium infantis)、ビフィドバクテリウム
・アドレセンティス(Bifidobacterium adolescentis
等が挙げられる。
The type of Bifidobacterium bacterium that can be used in the method of the present invention is not particularly limited. For example, Bifidobacterium breve (Bifidobacterium breve) may be used.
dobacterium breve), Bifidobacterium longum (Bifidobacterium longum), Bifidobacterium bifidum (Bifidobacterium bifidum), Bifidobacterium Animarisu (Bifidobacterium animal
is ), Bifidobacteriu
m suis ), Bifidobacterium infantis , Bifidobacterium adolescentis
And the like.

【0022】中でもビフィドバクテリウム・ブレーベ及
びビフィドバクテリウム・ロンガムは以前から乳製品に
数多く使用され安全性等のデータが積み重ねられてお
り、また、生残性の改善効果も高いため好ましい。
Among them, Bifidobacterium breve and Bifidobacterium longum have been used in dairy products for many years, and data such as safety have been accumulated.

【0023】上記のようにして得られるビフィドバクテ
リウム属細菌の培養液は、そのままあるいは他の甘味
料、果汁、香料、増粘剤などと組み合わせて飲食物とす
ることができる。その食品形態としては、特に発酵乳製
品、すなわち、牛乳、山羊乳等を乳酸菌により発酵させ
た飲料又は固形ヨーグルト等が好ましい。また、この他
にも賦形剤等を配合した錠菓、健康食品、医薬品等とし
て使用することも可能である。
The culture solution of the bacterium belonging to the genus Bifidobacterium obtained as described above can be used as a food or drink as it is or in combination with other sweeteners, fruit juices, flavors, thickeners and the like. The food form is preferably a fermented milk product, that is, a drink or solid yogurt obtained by fermenting milk, goat milk, or the like with lactic acid bacteria. In addition, they can also be used as tablet confections, health foods, pharmaceuticals, etc. containing excipients and the like.

【0024】また、ビフィドバクテリウム属細菌飲食品
として、発酵乳製品を製造する場合、乳酸菌を含有して
もよい。製品中に共存させる乳酸菌は特に限定されず、
ラクトバチルス・カゼイ、ラクトバチルス・アシドフィ
ルス、ラクトバチルス・ガセリ、ラクトバチルス・ヘル
ベティカス、ラクトバチルス・プランタラム、ラクトバ
チルス・デルブルッキィー、ラクトバチルス・クリスパ
タス、ラクトバチルス・ファーメンタム、ラクトバチル
ス・ロイテリ、ラクトバチルス・ゼアエ等のラクトバチ
ルス属細菌;ストレプトコッカス・サーモフィルス等の
ストレプトコッカス属細菌;エンテロコッカス・フェカ
ーリス、エンテロコッカス・フェンウム等のエンテロコ
ッカス属細菌;ラクトコッカス・ラクチス等のラクトコ
ッカス属細菌いずれも好適に使用することができ、特
に、風味や食経験に基づく安全性などの点から、ラクト
バチルス・ヘルベティカス、ラクトコッカス・ラクチ
ス、ラクトバチルス・ガセリ、ストレプトコッカス・サ
ーモフィルス、ラクトバチルス・カゼイ及びラクトバチ
ルス・アシドフィルスが好ましい。また、これら乳酸菌
とは別の微生物と併用して用いることも可能である。
In the case of producing a fermented milk product as a Bifidobacterium bacterium food or drink, it may contain lactic acid bacteria. The lactic acid bacteria coexisting in the product is not particularly limited,
Lactobacillus casei, Lactobacillus acidophilus, Lactobacillus gasseri, Lactobacillus helveticus, Lactobacillus plantarum, Lactobacillus delbruchy, Lactobacillus crispatas, Lactobacillus fermentum, Lactobacillus reuteri, Lact Lactobacillus bacteria such as Bacillus zeae; Streptococcus bacteria such as Streptococcus thermophilus; Enterococcus bacteria such as Enterococcus faecalis and Enterococcus phenum; Lactococcus bacteria such as Lactococcus lactis are preferably used. In particular, Lactobacillus helveticus, Lactococcus lactis, Lactobacillus Seri, Streptococcus thermophilus, Lactobacillus casei and Lactobacillus acidophilus is preferable. Further, these lactic acid bacteria can be used in combination with other microorganisms.

【0025】用いる工程の種類、すなわち溶存酸素量、
温度、浸透圧又はpHの変化を選ぶ際には、製品形態や設
計、作業性等を考慮して選択することが好ましい。例え
ば、糖などを加えないプレーンタイプの発酵乳等の製品
に用いる場合は、作業性等の点から溶存酸素量や温度を
変化させる工程を適用することが好ましい。
The type of process used, that is, the amount of dissolved oxygen,
When selecting a change in temperature, osmotic pressure, or pH, it is preferable to select the change in consideration of the product form, design, workability, and the like. For example, when used for products such as plain fermented milk to which no sugar or the like is added, it is preferable to apply a step of changing the amount of dissolved oxygen or the temperature from the viewpoint of workability and the like.

【0026】また、糖類を添加し、pHの高いタイプの発
酵乳等の製品を製造する場合は、浸透圧を変化させる工
程を適用し、pHの低い製品にはpHの低下の工程を用いれ
ば簡便に好適な生残性が得られる。
When a saccharide is added to produce a product such as fermented milk of a high pH type, a step of changing the osmotic pressure is applied. For a product of a low pH, a step of lowering the pH is used. Suitable survivability can be easily obtained.

【0027】更に、保存時には通気性容器、嫌気性容器
のどちらを使用してもよいが、嫌気性の容器を用いるこ
とがより好ましい。
Further, at the time of storage, either a gas-permeable container or an anaerobic container may be used, but it is more preferable to use an anaerobic container.

【0028】[0028]

【実施例】次に実施例を挙げ本発明を更に詳しく説明す
るが、本発明はこれら実施例になんら制約されるもので
はない。
Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples.

【0029】実施例1 溶存酸素量を増加させる方法による生残性改善効果 以下の方法にて、溶存酸素量を増加させる方法のビフィ
ドバクテリウム属細菌生残性改善効果を検討した。
Example 1 Survivability improving effect by increasing the amount of dissolved oxygen The effect of increasing the amount of dissolved oxygen on the survival of Bifidobacterium bacteria was examined by the following method.

【0030】すなわち、3リットル容コルベンに下に示
す乳培地を添加し、ビフィドバクテリウム・ブレーベY
IT4065株を1%接種した。綿栓をした後、34
℃、11〜12時間培養し、1.0×109/mlの培養
液を得た。この培養液のpHは5.7、浸透圧は560mO
sm、溶存酸素量は約1ppm であった。その後100rpm
で攪拌しながら4時間培養を継続したものと、2時間培
養した後に更に2時間攪拌を止めて培養した培養液を2
通り作製した。攪拌開始後120分後に培養液の浸透圧
及び溶存酸素量を測定したところ、約590mOsm、7.
5ppm であった。こうして得られた培養液は、いずれも
1.5×109/ml、pHは5.3であった。冷却したそ
れぞれの培養液に、冷パラチノース溶液を終濃度0.3
3モルとなるように添加し、ガラス製の試験管に充填し
空気に触れないようにブチル栓で密栓した。また、対照
として、培養中に攪拌せずに、1.5×109/mlまで
培養した培養液を用いた製品も同様に作製した。この様
にして得られた製品群の10℃保存時における7、1
4、21日の生残率を測定した。結果を表1に示す。
That is, a milk medium shown below was added to a 3-liter Kolben, and Bifidobacterium breve Y.
1% of the IT4065 strain was inoculated. After plugging the cotton, 34
° C., and incubated 11-12 hours to give a culture broth of 1.0 × 10 9 / ml. The pH of this culture is 5.7 and the osmotic pressure is 560 mO
sm and dissolved oxygen content were about 1 ppm. Then 100rpm
The culture was continued for 4 hours with agitation and the culture was cultured for 2 hours and then agitation was stopped for another 2 hours.
Prepared as follows. When the osmotic pressure and dissolved oxygen content of the culture solution were measured 120 minutes after the start of stirring, approximately 590 mOsm was obtained.
It was 5 ppm. All of the cultures thus obtained had a concentration of 1.5 × 10 9 / ml and a pH of 5.3. A cold palatinose solution was added to each of the cooled cultures to a final concentration of 0.3.
The solution was added to a concentration of 3 mol, filled in a glass test tube, and sealed with a butyl stopper so as not to be exposed to air. Further, as a control, a product using a culture solution cultured to 1.5 × 10 9 / ml without stirring during the culture was similarly prepared. 7, 10 when the product group obtained in this way was stored at 10 ° C.
The survival rate on days 4 and 21 was measured. Table 1 shows the results.

【0031】(乳培地組成) 全脂粉乳 520g 酵母エキス 0.75g 水 2100g *溶解後、135℃で5秒間、滅菌処理した。(Composition of milk medium) 520 g of whole milk powder, 0.75 g of yeast extract, 2100 g of water

【0032】[0032]

【表1】 [Table 1]

【0033】この結果から明らかなように、培養途中で
一定期間攪拌を行って製造した製品は、未攪拌で培養し
て製造した製品の場合よりも高い生残性を示していた。
As is clear from the results, the product manufactured by stirring for a certain period of time during the culturing showed higher survival than the product manufactured by culturing without stirring.

【0034】実施例2 温度を上昇させる方法による生残性改善効果 以下の方法にて、温度を上昇させる方法のビフィドバク
テリウム属細菌生残性改善効果を検討した。
Example 2 Survivability Improvement Effect by Increasing Temperature The effect of increasing the temperature on the survival of Bifidobacterium bacteria was examined by the following method.

【0035】すなわち、3L容コルベンに実施例1と同
じ乳培地を添加し、ビフィドバクテリウム・ブレーベY
IT4065株を1%接種した。綿栓をした後、34
℃、11〜12時間培養し、1.0×109/mlの培養
液を得た。この培養液のpHは5.7であった。この培養
液の温度を37、40、42℃の各温度に上昇させた
後、4時間培養を継続した培養液、及び42℃に昇温後
2時間培養してから34℃まで温度を下げ、更に2時間
培養した培養液を得た。これらの培養液は、菌数が1.
9cfu/ml、pH5.3であった。冷却した培養液に、冷
パラチノース溶液を終濃度0.33モルとなるように添
加し、ガラス製の試験管に充填し空気に触れないように
ブチル栓で密栓した。また、対照として、培養中に温度
を上昇させずに3.0×109/mlまで培養した培養液
を用いた製品も同様に作製した。この様にして得られた
製品群の10℃保存時における7、14、21日の生残
率を測定した。結果を表2に示す。
That is, the same milk medium as in Example 1 was added to a 3 L Kolben, and Bifidobacterium breve Y was added.
1% of the IT4065 strain was inoculated. After plugging the cotton, 34
° C., and incubated 11-12 hours to give a culture broth of 1.0 × 10 9 / ml. The pH of this culture was 5.7. After raising the temperature of the culture solution to each of 37, 40, and 42 ° C., the culture solution continued to be cultured for 4 hours, and the temperature was raised to 42 ° C., followed by culturing for 2 hours, and then the temperature was lowered to 34 ° C. A culture solution cultured for another 2 hours was obtained. These cultures have a bacterial count of 1.
5 9 cfu / ml, it was pH 5.3. A cold palatinose solution was added to the cooled culture solution to a final concentration of 0.33 mol, filled in a glass test tube, and sealed with a butyl stopper so as not to be exposed to air. Further, as a control, a product using a culture solution cultured to 3.0 × 10 9 / ml without increasing the temperature during the culture was similarly prepared. The survival rates of the product group obtained in this way at 7, 14 and 21 days when stored at 10 ° C. were measured. Table 2 shows the results.

【0036】[0036]

【表2】 [Table 2]

【0037】この結果から明らかなように、培養途中で
培養温度を34℃から37、42℃に上昇させて製造し
た製品は、34℃一定で培養して製造した製品よりも高
い生残性を示していた。処理温度は37℃よりも42℃
の方が、また処理時間は2時間より4時間の方がより高
い生残性を示した。
As is apparent from the results, the product produced by increasing the culture temperature from 34 ° C. to 37 or 42 ° C. during the cultivation has a higher survivability than the product produced by culturing at a constant 34 ° C. Was showing. Processing temperature is 42 ° C rather than 37 ° C
, And the treatment time was higher at 4 hours than at 2 hours.

【0038】実施例3 浸透圧を上昇させる方法による生残性改善効果 以下の方法にて、浸透圧を上昇させる方法のビフィドバ
クテリウム属細菌生残性改善効果を検討した。
Example 3 Survivability Improvement Effect by Osmotic Pressure Raising Method The effect of increasing the osmotic pressure on the viability of Bifidobacterium bacteria was examined by the following method.

【0039】すなわち、3L容コルベンに実施例1と同
じ乳培地を添加し、ビフィドバクテリウム・ブレーベY
IT4065株を1%接種した。綿栓をした後、34
℃、11〜12時間培養し、1.0×109/mlの培養
液を得た。この培養液のpHは5.7また浸透圧は約64
0mOsmであった。この培養液に34℃に加温したパラチ
ノース溶液(約1300mOsm)を終濃度0.33モルと
なるように添加した後、4時間培養を継続し、3.0×
109/mlの培養液を得た。この培養液のpHは5.4、
浸透圧は約950mOsmであった。冷却した培養液を、ガ
ラス製の試験管に充填し空気に触れないようにブチル栓
で密栓した。また、対照として、培養中にパラチノース
溶液を添加せずに3.0×109/mlまで培養した培養
液に、冷パラチノース溶液を添加した製品も作製した。
この様にして得られた製品群の10℃保存時における
7、14、21日の生残率を測定した。結果を表3に示
す。
That is, the same milk medium as in Example 1 was added to a 3 L Kolben, and Bifidobacterium breve Y.
1% of the IT4065 strain was inoculated. After plugging the cotton, 34
° C., and incubated 11-12 hours to give a culture broth of 1.0 × 10 9 / ml. The pH of this culture was 5.7 and the osmotic pressure was about 64.
It was 0 mOsm. After adding a palatinose solution (about 1300 mOsm) heated to 34 ° C. to this culture solution to a final concentration of 0.33 mol, the culture was continued for 4 hours, and 3.0 ×
A 10 9 / ml culture was obtained. The pH of this culture was 5.4,
The osmotic pressure was about 950 mOsm. The cooled culture solution was filled in a glass test tube, and sealed with a butyl stopper so as not to be exposed to air. As a control, a product was also prepared in which a cold palatinose solution was added to a culture solution cultured to 3.0 × 10 9 / ml without adding a palatinose solution during the culture.
The survival rates of the product group obtained in this way at 7, 14 and 21 days when stored at 10 ° C. were measured. Table 3 shows the results.

【0040】[0040]

【表3】 [Table 3]

【0041】この結果から明らかなように、培養途中で
温パラチノース溶液を添加し、浸透圧を上昇させて製造
した製品は、浸透圧を上昇させずに培養して製造した製
品の場合よりも高い生残性を示していた。
As is clear from the results, the product produced by adding the warm palatinose solution during the cultivation and increasing the osmotic pressure is higher than the product produced by culturing without increasing the osmotic pressure. Showed survivability.

【0042】実施例4 培養液のpHを変化させる方法による生残性改善効果 以下の方法にて、培養液のpHを変化させる工程のビフィ
ドバクテリウム属細菌生残性改善効果を検討した。すな
わち、3リットル容コルベンに下に実施例1と同じ乳培
地を添加し、ビフィドバクテリウム・ブレーベYIT4
065株を1%接種した。綿栓をした後、34℃、11
〜12時間培養し、1.0×109/mlの培養液を得
た。この培養液のpHは5.7であった。2Mリンゴ酸溶
液を用いて培養液のpHを4.4、5.4に低下させ34
℃にて4時間培養を継続した。pH4.4のもののみ培養
2時間の培養液も得た。いずれも菌数1.5×109/m
lの培養液であった。冷却したそれぞれの培養液に2M
水酸化ナトリウム溶液を添加しpHを5.3とした後、冷
パラチノース溶液を終濃度0.33モルとなるように添
加し、ガラス製の試験管に充填し空気に触れないように
ブチル栓で密栓した。また、対照として、pHを変化させ
る処理を施さずに1.5×109/mlまで培養した培養
液を用いた製品も同様に作製した。この様にして得られ
た製品群の10℃保存時における7、14、21日の生
残率を測定した。結果を表4に示す。
Example 4 Effect of Improving Survivability by Changing pH of Culture Solution The effect of improving the viability of Bifidobacterium bacteria in the step of changing the pH of the culture solution was examined by the following method. That is, the same milk medium as in Example 1 was added to a 3-liter Kolben, and Bifidobacterium breve YIT4 was added.
065 strains were inoculated at 1%. After plugging the cotton, 34 ℃, 11
After culturing for 1212 hours, a culture solution of 1.0 × 10 9 / ml was obtained. The pH of this culture was 5.7. The pH of the culture was reduced to 4.4, 5.4 using a 2M malic acid solution and
The culture was continued at 4 ° C. for 4 hours. A culture solution for 2 hours of culture was also obtained only for those having a pH of 4.4. In all cases, the number of bacteria is 1.5 × 10 9 / m
l of culture. 2M each chilled culture
After adding sodium hydroxide solution to adjust the pH to 5.3, a cold palatinose solution was added to a final concentration of 0.33 mol, filled in a glass test tube, and sealed with a butyl stopper so as not to be exposed to air. Sealed. Further, as a control, a product using a culture solution cultured to 1.5 × 10 9 / ml without performing a treatment for changing the pH was similarly prepared. The survival rates of the product group obtained in this way at 7, 14 and 21 days when stored at 10 ° C. were measured. Table 4 shows the results.

【0043】[0043]

【表4】 [Table 4]

【0044】表4から明らかなように、培養途中にpHを
低下させ製造した製品は、対照よりも高い生残性を示し
ていた。処理後のpHは5.4よりも4.4の方が、また
処理時間は2時間より4時間の方が高い生残性を示し
た。
As is evident from Table 4, the products produced by lowering the pH during the cultivation showed higher survival than the control. The pH after treatment was higher at 4.4 than at 5.4, and the survival time was higher at 4 hours than at 2 hours.

【0045】実施例5 浸透圧を上昇させる工程による生残性改善効果 以下の方法にて、浸透圧を上昇させる工程のビフィドバ
クテリウム属細菌生残性改善効果を検討した。
Example 5 Effect of Improving Survivability by Step of Increasing Osmotic Pressure The effect of improving the survival of Bifidobacterium bacteria by the step of increasing osmotic pressure was examined by the following method.

【0046】すなわち、3リットル容コルベンに実施例
1と同じ乳培地を添加し、ビフィドバクテリウム・ブレ
ーベYIT4065株を1%接種した。綿栓をした後、
34℃、11〜12時間培養し、1.0×109/mlの
培養液を得た。この培養液のpHは5.7また浸透圧は約
590mOsmであった。この培養液に34℃に加温した1
Mパラチノース溶液を培地の浸透圧との差が74、13
4、230、262、353mOsmとなるように添加した
後、4時間培養を継続し、1.5×109/mlの培養液
を得た。この培養液のpHは5.3であった。冷却したそ
れぞれの培養液に冷却した1Mパラチノース溶液をいず
れも0.33Mとなるように添加した後、ガラス製の試
験管に充填し空気に触れないようにブチル栓で密栓し
た。また、対照として、培養中にパラチノース溶液を添
加せずに1.5×109/mlまで培養した培養液に、冷
パラチノース溶液を添加した製品も作製した。この様に
して得られた製品群の10℃保存時における7、14、
21日の生残率を測定した。結果を表5に示す。
That is, the same milk medium as in Example 1 was added to a 3 liter Kolben, and 1% of Bifidobacterium breve strain YIT4065 was inoculated. After plugging the cotton,
Culture was performed at 34 ° C. for 11 to 12 hours to obtain a culture solution of 1.0 × 10 9 / ml. The pH of this culture was 5.7 and the osmotic pressure was about 590 mOsm. This culture was heated to 34 ° C.
The difference between the M palatinose solution and the osmotic pressure of the medium was 74, 13
After the addition of 4, 230, 262, and 353 mOsm, the culture was continued for 4 hours to obtain a culture solution of 1.5 × 10 9 / ml. The pH of this culture was 5.3. After adding the cooled 1M palatinose solution to each of the cooled culture solutions to a concentration of 0.33M, the mixture was filled in a glass test tube and sealed with a butyl stopper so as not to be exposed to air. Further, as a control, a product was also prepared in which a cold palatinose solution was added to a culture solution cultured to 1.5 × 10 9 / ml without adding a palatinose solution during the culture. 7, 14 when the product group thus obtained was stored at 10 ° C.
The 21-day survival rate was measured. Table 5 shows the results.

【0047】[0047]

【表5】 [Table 5]

【0048】表5から明らかなように、浸透圧差が13
4を超えると、対照よりも高い生残性を示していた。
As is clear from Table 5, the osmotic pressure difference was 13
Above 4, it showed higher survival than the control.

【0049】実施例6 溶存酸素量を増加させる方法による生残性改善効果 菌株としてビフィドバクテリウム・ロンガムYIT40
21を用いた以外は実施例1と同様の条件で、溶存酸素
量の生残性への影響を検討した。その結果ビフィドバク
テリウム・ロンガムでも同様に生残性改善効果が得られ
た。
Example 6 Survival-improving effect by increasing the amount of dissolved oxygen Bifidobacterium longum YIT40 as a strain
Under the same conditions as in Example 1 except that 21 was used, the effect of the dissolved oxygen amount on the survival was examined. As a result, Bifidobacterium longum also exhibited a survival improvement effect.

【0050】実施例7 以下の基本培養条件に各種の条件を適用して発酵乳を調
製し、保存時の生残性を比較した。 (基本条件)粉乳420gとミースト(アサヒビール社
製)0.6gを水1700gに溶解し、135℃で3.
5秒間滅菌したものを3リットル容コルベンに2L分注
し、乳培地とした。この乳培地に、ビフィドバクテリウ
ム・ブレーベYIT4064株を1%、ラクトバチルス
・ガセリYIT0168を0.1%接種した。綿栓した
後、34℃でビフィドバクテリウム・ブレーベの菌数が
1.5×109となるまで培養し、培養液とした。この
培養液を10℃に冷却し、4℃の1Mグルコース溶液1
Lと混合し、均質化機で150kg/cm2 の圧力で均質化
し発酵乳とした。こうして得られる発酵乳(コントロー
ル)と以下の各種条件を具備したサンプルを調製した。 実施品1:培養終了4時間前から2時間攪拌を行い、攪
拌中は培養液の溶存酸素が飽和状態になるように維持し
た。 実施品2:培養終了4時間前から培養終了まで培養温度
を42℃に維持した 実施品3:培養液と1Mグルコース溶液との混合を34
℃で行った。 実施品4:ビフィドバクテリウム・ブレーベの菌数が2
×108 の段階でクエン酸を添加し、pHを1.0低下さ
せ2時間維持した後、水酸化ナトリウム溶液で元のpHに
戻し、培養を継続した。 実施品5:培養終了4時間前に1Mグルコース溶液との
混合を攪拌しながら42℃で行い、培養終了まで攪拌及
び42℃恒温を継続した。 こうして得られた発酵乳をガラス瓶に充填、密封し、1
0℃で21日間静置保存した。結果を表6に示す。
Example 7 Fermented milk was prepared by applying various conditions to the following basic culture conditions, and the survival characteristics during storage were compared. (Basic conditions) 420 g of milk powder and 0.6 g of a mist (manufactured by Asahi Breweries, Ltd.) are dissolved in 1700 g of water.
Two liters of the sterilized solution for 5 seconds were dispensed into a 3-liter Kolben to obtain a milk medium. This milk medium was inoculated with 1% of Bifidobacterium breve YIT4064 strain and 0.1% of Lactobacillus gasseri YIT0168. After the cotton plug was inserted, the cells were cultured at 34 ° C. until the number of Bifidobacterium breve reached 1.5 × 10 9 to obtain a culture solution. The culture was cooled to 10 ° C., and 1M glucose solution 1 at 4 ° C.
L and homogenized with a homogenizer at a pressure of 150 kg / cm 2 to obtain fermented milk. The fermented milk (control) thus obtained and samples having the following various conditions were prepared. Example 1: Stirring was performed for 2 hours from 4 hours before the end of the culturing, and the dissolved oxygen in the culture was maintained in a saturated state during the stirring. Example 2: The culture temperature was maintained at 42 ° C from 4 hours before the end of the culture to the end of the culture. Example 3: Mixing of the culture solution and the 1M glucose solution was performed for 34 hours.
C. was performed. Example 4: Bifidobacterium breve has a bacterial count of 2
At the stage of × 10 8 , citric acid was added to lower the pH by 1.0 and maintained for 2 hours, then returned to the original pH with sodium hydroxide solution, and the culture was continued. Example 5: Four hours before the end of the culture, mixing with a 1 M glucose solution was performed at 42 ° C. with stirring, and stirring and constant temperature at 42 ° C. were continued until the end of the culture. The fermented milk thus obtained is filled in a glass bottle, sealed, and
It was stored at 0 ° C. for 21 days. Table 6 shows the results.

【0051】[0051]

【表6】 [Table 6]

【0052】表6から明らかなとおり、ビフィドバクテ
リウム属細菌の代謝を停止させずに増殖速度を低下させ
る工程を具備することで、優れた生残性を有する発酵乳
を製造できることがわかった。特に培養終了時から4時
間程度前までに該工程を適用した場合の生残性改善効果
が優れていた。また、本品は21日保存後でも色調変
化、分離、沈殿等はほとんど見られず、良好な安定性を
示した。更に、本品は、官能面でも全く問題ない優れた
風味を有していた。
As is clear from Table 6, fermented milk having excellent survivability can be produced by providing the step of reducing the growth rate without stopping the metabolism of Bifidobacterium bacteria. . In particular, the effect of improving the survivability when this step was applied up to about 4 hours before the end of the culture was excellent. This product showed good stability with almost no change in color tone, separation, precipitation, etc. even after storage for 21 days. Furthermore, this product had an excellent flavor which had no problem in terms of sensory aspects.

【0053】実施例8 発酵乳の製造 3リットル容コルベンに全脂粉乳520gとミースト
(アサヒビール社製)0.75gを水2100gに溶解
し、135℃で5秒間滅菌し、乳培地とした。この乳培
地に、ビフィドバクテリウム・ブレーベYIT4065
株を1%、ラクトバチルス・アシドフィルスを0.1%
接種した。綿栓をした後、34℃、11〜12時間培養
し、1.0×109/mlの培養液を得た。この培養液に
34℃に加温した1Mパラチノース溶液0.84Lを添
加した後、4時間培養を継続した。2.0×109/ml
の培養液を得た。この培養液を均質機にかけ均質化した
ものを発酵乳とした。この発酵乳のpHは5.4、乳酸菌
数は5×107/ml、ビフィズス菌数は1×109/mlで
あった。
Example 8 Production of Fermented Milk 520 g of whole milk powder and 0.75 g of mast (manufactured by Asahi Breweries) were dissolved in 2100 g of water in a 3 liter kolben, and sterilized at 135 ° C. for 5 seconds to prepare a milk medium. In this milk medium, Bifidobacterium breve YIT4065 was added.
1% strain, 0.1% Lactobacillus acidophilus
Inoculated. After stoppering with a cotton plug, the mixture was cultured at 34 ° C. for 11 to 12 hours to obtain a culture solution of 1.0 × 10 9 / ml. After 0.84 L of a 1 M palatinose solution heated to 34 ° C. was added to the culture, the culture was continued for 4 hours. 2.0 × 10 9 / ml
Was obtained. This culture solution was homogenized by a homogenizer and used as fermented milk. The pH of this fermented milk was 5.4, the number of lactic acid bacteria was 5 × 10 7 / ml, and the number of bifidobacteria was 1 × 10 9 / ml.

【0054】[0054]

【発明の効果】本発明により、ビフィドバクテリウム属
細菌の代謝を停止させずに増殖速度を低下させる工程を
単独もしくは組み合わせてビフィドバクテリウム属細菌
の培養時に導入すれば、ビフィドバクテリウム属細菌の
生残性を改善し、摂取時の生理効果を高めることが可能
となる。また、本発明方法によって得られた培養液又は
培養物は良好な風味を有しており、多種類の飲食品に用
いることができる。
According to the present invention, if the step of reducing the growth rate without stopping the metabolism of Bifidobacterium is introduced alone or in combination during the culture of Bifidobacterium, It is possible to improve the viability of the genus bacteria and enhance the physiological effect upon ingestion. Moreover, the culture solution or culture obtained by the method of the present invention has a good flavor and can be used for various kinds of foods and drinks.

フロントページの続き (72)発明者 三浦 みか 東京都港区東新橋1丁目1番19号 株式会 社ヤクルト本社内 (72)発明者 池邨 治夫 東京都港区東新橋1丁目1番19号 株式会 社ヤクルト本社内 (72)発明者 森下 ▼隆▲ 東京都港区東新橋1丁目1番19号 株式会 社ヤクルト本社内 Fターム(参考) 4B001 AC02 AC30 AC31 AC50 AC99 BC03 BC14 EC05 4B018 LB07 LB08 LE04 LE05 MD28 MD29 MD81 MD86 MD87 ME02 ME11 MF13 4B065 AA21X BB15 BB16 BB24 BB29 BC01 BC02 BC03 BC14 BC50 BD07 BD12 BD36 CA42Continuing from the front page (72) Inventor Mika Miura 1-1-19 Higashi-Shimbashi, Minato-ku, Tokyo Yakult Honsha Co., Ltd. (72) Inventor Haruo Ikeson 1-1-19, Higashi-Shimbashi, Minato-ku, Tokyo Stock Yakult Honsha (72) Inventor Morishita ▼ Takashi ▲ 1-1-19 Higashi-Shimbashi, Minato-ku, Tokyo F-term (reference) 4B001 AC02 AC30 AC31 AC50 AC99 BC03 BC14 EC05 4B018 LB07 LB08 LE04 LE05 MD28 MD29 MD81 MD86 MD87 ME02 ME11 MF13 4B065 AA21X BB15 BB16 BB24 BB29 BC01 BC02 BC03 BC14 BC50 BD07 BD12 BD36 CA42

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ビフィドバクテリウム属細菌の培養途中
に、該細菌の代謝を停止させずに増殖速度を低下させる
工程を導入することを特徴とするビフィドバクテリウム
属細菌含有飲食品の製造方法。
1. A method for producing a Bifidobacterium-containing bacterium-containing food or drink, wherein a step of reducing the growth rate without stopping the metabolism of the Bifidobacterium bacterium is introduced during the cultivation of the bacterium of the genus Bifidobacterium. Method.
【請求項2】 ビフィドバクテリウム属細菌の代謝を停
止させずに増殖速度を低下させる工程が次の(a)〜
(d) (a)培養液中の溶存酸素量を増加させる工程 (b)培養液の温度を変化させる工程 (c)培養液の浸透圧を変化させる工程 (d)培養液のpHを変化させる工程 から選ばれる1又は2以上である請求項1記載の製造方
法。
2. The step of reducing the growth rate without stopping the metabolism of Bifidobacterium bacteria includes the following steps (a) to (a):
(D) (a) a step of increasing the amount of dissolved oxygen in the culture solution (b) a step of changing the temperature of the culture solution (c) a step of changing the osmotic pressure of the culture solution (d) changing the pH of the culture solution The production method according to claim 1, wherein the method is one or more selected from the steps:
【請求項3】 ビフィドバクテリウム属細菌の代謝を停
止させずに増殖速度を低下させる工程が次の(a)〜
(d) (a)培養途中の溶存酸素量を3ppm 乃至飽和状態にま
で増加させる工程 (b)培養液の温度を元の培養温度から3〜14℃変化
させる工程 (c)培養液の浸透圧を元の浸透圧から150〜800
mOsm変化させる工程 (d)培養液のpHを元のpHから0.3〜3変化させる工
程 から選ばれる1又は2以上である請求項1記載の製造方
法。
3. The step of reducing the growth rate without stopping the metabolism of Bifidobacterium bacterium includes the following steps (a) to (a):
(D) (a) a step of increasing the amount of dissolved oxygen during the culture from 3 ppm to a saturated state (b) a step of changing the temperature of the culture solution from 3 to 14 ° C. from the original culture temperature (c) the osmotic pressure of the culture solution 150-800 from the original osmotic pressure
2. The method according to claim 1, wherein the step of changing the mOsm is one or more selected from (d) a step of changing the pH of the culture solution by 0.3 to 3 from the original pH.
【請求項4】 請求項1、2又は3記載の方法により得
られたビフィドバクテリウム属細菌を含有する飲食品。
4. A food or drink containing a bacterium belonging to the genus Bifidobacterium obtained by the method according to claim 1, 2 or 3.
JP29530099A 1999-10-18 1999-10-18 Production of food and drink containing bacteria of genus bifidobacterium Pending JP2001112437A (en)

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