JP2005087193A - Reducing fermented milk and method for producing the same - Google Patents

Reducing fermented milk and method for producing the same Download PDF

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JP2005087193A
JP2005087193A JP2003363838A JP2003363838A JP2005087193A JP 2005087193 A JP2005087193 A JP 2005087193A JP 2003363838 A JP2003363838 A JP 2003363838A JP 2003363838 A JP2003363838 A JP 2003363838A JP 2005087193 A JP2005087193 A JP 2005087193A
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fermented milk
hydrogen gas
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Wataru Murota
渉 室田
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Abstract

<P>PROBLEM TO BE SOLVED: To obtain fermented milk economically producible with a small-sized production apparatus and having low oxidation-reduction potential and extremely strong reducibility. <P>SOLUTION: The reducing fermented milk is obtained by dissolving hydrogen gas at -180°C to 90°C in fermented milk at 0-100°C through applying pressure of 0.1-1,000 atm and returning the product to normal temperature and normal pressure. Since the reducing fermented milk has extremely low oxidation-reduction potential, the fermented milk causes no health problem and can be ordinarily used as reducing fermented milk. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

この出願の発明は、新規な還元性発酵乳及びその製造方法に関する。  The invention of this application relates to a novel reducing fermented milk and a method for producing the same.

従来から、発酵乳は健康促進を考えて一般的に広く飲用されるものであるが、その発酵乳を酸化還元という立場から検証する考え方はない。通常いろいろな発酵乳が、通常の生活の中で取り入れられているが、その飲用する発酵乳の酸化還元電位を問題視し、発酵乳に還元性を持たせようとする考え方はあまり取り入れられてこなかった。  Conventionally, fermented milk is generally drunk in consideration of health promotion, but there is no way to verify the fermented milk from the standpoint of redox. Various types of fermented milk are usually incorporated in daily life, but the idea of giving fermented milk a reducibility is often taken into account, considering the oxidation-reduction potential of the fermented milk that is consumed. There wasn't.

そこで、発明者は、還元性の発酵乳を得るべくいろいろな実験を重ねた結果、発酵乳に加圧下で常温ないし冷却した水素ガスを平衡状態となるまで溶解させ、この状態で加圧圧力を取り除いて常温常圧に戻すと、溶解していた水素ガスの一部分が気化するとはいえ、通常の溶解度の数倍ないし数千倍近い水素ガスが溶解していること、この溶解した水素ガスは、ほとんど気化することなく安定して溶解しているため、非常に低い酸化還元電位を有することを見出し、本願発明を完成するに至ったのである。  Therefore, the inventor conducted various experiments to obtain reducible fermented milk, and as a result, dissolved hydrogen gas that had been cooled to room temperature or cooled under pressure until it reached an equilibrium state. When it is removed and returned to room temperature and normal pressure, a part of the dissolved hydrogen gas is vaporized, but the hydrogen gas is dissolved several times to several thousand times the normal solubility. The present inventors have found that it has a very low redox potential because it is stably dissolved with little vaporization, and has completed the present invention.

すなわち、本発明は、十分な還元性を有する発酵乳及びその製造方法を提供することを目的とする。本発明のかかる目的は以下の構成により達成し得る。  That is, an object of the present invention is to provide fermented milk having sufficient reducing ability and a method for producing the same. This object of the present invention can be achieved by the following configurations.

本発明の一態様によれば、常温常圧下で酸化還元電位が−10mv以下の発酵乳が提供される。この還元性の発酵乳はこれまでに飲用に供されてきた発酵乳と違い、十分に低い−10mv以下の酸化還元電位を有しているため、何らの健康問題を引き起こすこともなく、還元性発酵乳として通常的に飲用することができることになる。  According to one embodiment of the present invention, fermented milk having a redox potential of −10 mV or less under normal temperature and normal pressure is provided. This fermented fermented milk has a sufficiently low oxidation-reduction potential of −10 mV or less, unlike fermented milk that has been used for drinking so far, and does not cause any health problems. It can be normally drunk as fermented milk.

また、本発明の別の態様によれば、0℃〜100℃の発酵乳に−180℃〜90℃の水素ガスを0.1気圧〜1000気圧に加圧して溶解せしめ、常温常圧に戻すことにより得られた還元性発酵乳及びその製造方法が提供される。  Moreover, according to another aspect of the present invention, hydrogen gas of −180 ° C. to 90 ° C. is pressurized to 0.1 atm to 1000 atm in fermented milk at 0 ° C. to 100 ° C. and returned to normal temperature and normal pressure. The reduced fermented milk obtained by this and its manufacturing method are provided.

なお、本発明における還元性発酵乳の製造に際し、水素ガスの温度の上限を90℃としたのは、水素ガスは通常水素ガスボンベ内に入れられて供給されるが、室外に放置されていた水素ガスボンベの温度が太陽光により90℃となることはよくあることであり、この程度の水素ガスでも十分に発酵乳に溶解させることができるが、あまり温度が高いものでは発酵乳の温度の著しい上昇につながって溶解度が減少するので好ましくないためである。水素ガスの温度の下限を−180℃としたのは、水素ガスは−253℃以下に冷却された液体水素の形で供給される場合もあるが、この液体水素を気化させて発酵乳に溶解させる際、もとの発酵乳の温度、水素ガスの供給圧力及び流量にも依存するが、実験的に発酵乳が凝固しないように溶解させ得る温度を確認して限定したものである。しかしながら、得られる還元性発酵乳は最終的には常温常圧に戻されるものであるから、経済性及びエネルギー効率の観点からは、液体水素の有する低温を他の目的に利用して、発酵乳に溶解させる際の水素温度は0℃以上となしたほうがよい。  In the production of the reduced fermented milk in the present invention, the upper limit of the temperature of the hydrogen gas was set to 90 ° C. The reason why the hydrogen gas is usually supplied in a hydrogen gas cylinder, but the hydrogen gas left in the room It is common for the temperature of gas cylinders to reach 90 ° C. due to sunlight, and even this level of hydrogen gas can be sufficiently dissolved in fermented milk, but if the temperature is too high, the temperature of fermented milk will rise significantly. This is because it is not preferable because the solubility is reduced. The reason why the lower limit of the temperature of the hydrogen gas is set to −180 ° C. is that hydrogen gas may be supplied in the form of liquid hydrogen cooled to −253 ° C. or less, but this liquid hydrogen is vaporized and dissolved in fermented milk. Although it depends on the temperature of the original fermented milk, the supply pressure and flow rate of hydrogen gas, the temperature at which the fermented milk can be dissolved experimentally so as not to coagulate is limited. However, since the obtained reduced fermented milk is finally returned to normal temperature and normal pressure, from the viewpoint of economy and energy efficiency, the low temperature of liquid hydrogen is utilized for other purposes, and fermented milk is used. It is better that the hydrogen temperature when dissolved in is 0 ° C. or higher.

なお、発酵乳に水素ガスを溶解させる際の圧力は0.1気圧〜1000気圧(ゲージ圧)とする。圧力が高ければ高いほど発酵乳に溶解する水素ガス量は多くなるが、得られる還元性発酵乳は最終的には常温常圧に戻されるものであるから、あまり圧力が高くても常圧に戻した際に気化してしまう水素量が多くなるために経済的及びエネルギー的には無駄になる。好ましくは0.1気圧〜10気圧、更に好ましくは1気圧〜8気圧が使用される。  In addition, the pressure at the time of dissolving hydrogen gas in fermented milk shall be 0.1 atmosphere-1000 atmospheres (gauge pressure). The higher the pressure, the more hydrogen gas will dissolve in the fermented milk, but the resulting reduced fermented milk will eventually be returned to room temperature and normal pressure. Since the amount of hydrogen that is vaporized when returned is increased, it is wasted economically and in energy. Preferably 0.1 to 10 atmospheres, more preferably 1 to 8 atmospheres is used.

このとき、発酵乳への水素ガスの溶解割合は、水素ガスを溶解させた際の温度及び圧力により変化するが、常温常圧に戻した際に約0.001〜0.5wt%程度が安定して溶解している。常温常圧下における水素ガスの発酵乳への溶解度は約2ml/100ml(約1.8×10−4wt%)であるから、本発明で得られる還元性発酵乳中の水素ガス量は単に常温常圧下で水素ガスを溶解させた場合と比すると約5〜2500倍もの水素ガスが溶解していることになる。  At this time, the proportion of hydrogen gas dissolved in the fermented milk changes depending on the temperature and pressure when the hydrogen gas is dissolved, but about 0.001 to 0.5 wt% is stable when the temperature is returned to normal temperature and pressure. And dissolved. Since the solubility of hydrogen gas in fermented milk under normal temperature and normal pressure is about 2 ml / 100 ml (about 1.8 × 10 −4 wt%), the amount of hydrogen gas in the reduced fermented milk obtained in the present invention is simply normal temperature. Compared with the case where hydrogen gas is dissolved under pressure, about 5 to 2500 times as much hydrogen gas is dissolved.

このように多量の水素ガスが安定的に発酵乳中に溶解していることの理由は、水素ガスの一部分は過飽和状態で溶解していると考えることはできるが、それだけでは溶解水素ガス量が多すぎるために説明ができない。詳細な理由は今後の研究に待つ必要はあるが、本発明者は以下のような現象が生じているものと推定した。  The reason why such a large amount of hydrogen gas is stably dissolved in the fermented milk can be considered that a part of the hydrogen gas is dissolved in a supersaturated state. There is too much to explain. Although it is necessary to wait for further research for the detailed reason, the present inventor presumed that the following phenomenon occurred.

すなわち、常温常圧下で発酵乳に水素ガスを溶解させても、通常は何らの反応も生じない。しかしながら、加圧下で水素ガスを発酵乳に溶解させると発酵乳中の酸素原子と水素ガスの水素原子とが近づき、両者間に水素結合が生じ、そのため、加圧下では水素ガスは従来予測されているよりも多量に溶解する。この一旦生成した水素結合は常圧に戻しても幾分かは安定状態で残っているため、常圧下でも予測数量よりも数倍〜数千倍もの水素ガスが安定的に溶解しているものと推定される。  That is, even if hydrogen gas is dissolved in fermented milk at room temperature and normal pressure, no reaction usually occurs. However, when hydrogen gas is dissolved in fermented milk under pressure, the oxygen atoms in the fermented milk and the hydrogen atoms of hydrogen gas approach each other and hydrogen bonds are formed between them. Dissolves more than it does. This hydrogen bond once generated remains in a stable state even when it is returned to normal pressure, so hydrogen gas that is several to several thousand times more stable than the expected quantity is dissolved even under normal pressure. It is estimated to be.

本発明における還元性発酵乳の製造にあたっては、周知の気液接触装置を使用することができ、バッチ式であっても連続流通式であっても適宜使用し得る。高圧で水素ガスを吸収させた発酵乳を常温常圧に戻したときに気化した水素ガスは、当然に回収して再利用することができる。以下、本発明の具体例により詳細に説明する。  In producing the reduced fermented milk in the present invention, a well-known gas-liquid contact device can be used, and it can be appropriately used regardless of whether it is a batch type or a continuous flow type. Naturally, the hydrogen gas vaporized when the fermented milk that has absorbed hydrogen gas at high pressure is returned to normal temperature and pressure can be recovered and reused. Hereinafter, specific examples of the present invention will be described in detail.

(実施例)  (Example)

まず、水素ガスを溶解させる前の発酵乳のpH及び酸化還元電位を測定した。その結果を表にまとめて示した。  First, the pH and redox potential of fermented milk before dissolving hydrogen gas were measured. The results are summarized in a table.

実施例として室温における発酵乳に常温の水素ガスを入口圧力6気圧、出口圧力0.2気圧となるように調整し、気液接触装置を用い、計1リットルを200ml/分の割合で5分間流した。その後、得られた還元性発酵乳を常温常圧下に保持し、酸化還元電位及びpHを測定した。その結果をまとめて表に示した。  As an example, normal temperature hydrogen gas is adjusted to fermented milk at room temperature so that the inlet pressure is 6 atm and the outlet pressure is 0.2 atm. Washed away. Thereafter, the obtained reduced fermented milk was kept at room temperature and normal pressure, and the redox potential and pH were measured. The results are summarized in the table.

Figure 2005087193
(酸化還元電位及びpH測定については、共に東亜DKK製ORP計測器及びpH計測器を用いた)
この表の結果から、本発明の還元性発酵乳はpHがあまり変化しないにもかかわらず酸化還元電位が−541mvと非常に低い還元性を示しているのがわかる。
Figure 2005087193
(For redox potential and pH measurement, both ORP measuring instrument and pH measuring instrument made by Toa DKK were used)
From the results of this table, it can be seen that the reduced fermented milk of the present invention shows a reducibility that is very low at a redox potential of -541 mv, even though the pH does not change much.

Figure 2005087193
この表2の結果によれば、本発明に従って得られた還元性発酵乳を密閉容器内に保存すると徐々に酸化還元電位の値が低下して約24時間〜48時間後に極小値をとった後、徐々に上降する傾向がみられた。特にこのような電位変化が生じる理由については現在のところまだ解明されていないが、後半の酸化還元電位の上昇については容器内への周囲空気の進入の影響も考えられなくないので、別途、密閉容器を開放した場合の酸化還元電位の経時変化を確認することとした。
Figure 2005087193
According to the results in Table 2, after the reduced fermented milk obtained according to the present invention is stored in a closed container, the value of the oxidation-reduction potential gradually decreases and takes a minimum value after about 24 to 48 hours. There was a tendency to descend gradually. In particular, the reason why such a potential change occurs has not yet been elucidated at present. However, the increase in the second half of the redox potential cannot be considered due to the ingress of ambient air into the container. It was decided to confirm the change with time of the oxidation-reduction potential when the container was opened.

表1における酸化還元電位−541mvの還元性発酵乳を室温下に放置し、経過時間と酸化還元電位及びpHの関係を測定した。その結果をまとめて表3に示す。  Reducing fermented milk having a redox potential of -541 mv in Table 1 was allowed to stand at room temperature, and the relationship between elapsed time, redox potential, and pH was measured. The results are summarized in Table 3.

Figure 2005087193
この表3の結果によれば、本発明に従って得られた還元性発酵乳は開放容器にて保存するとpHにほとんど変化を及ぼさずに、酸化還元電位のみ上昇することがわかる。以上の表から推測すると発酵乳中に溶解していた水素ガスが気化してしまうというよりも、空気中の酸素が溶け込むことにより酸化還元電位が上昇すると考えられる。
Figure 2005087193
According to the results in Table 3, it can be seen that the reduced fermented milk obtained in accordance with the present invention increases only the oxidation-reduction potential with little change in pH when stored in an open container. Presuming from the above table, it is considered that the oxidation-reduction potential rises as oxygen in the air dissolves rather than the hydrogen gas dissolved in the fermented milk evaporates.

発明の効果The invention's effect

以上述べたように、本発明によれば、常温常圧下で酸化還元電位が非常に低い発酵乳が得られるので、何ら健康問題を引き起こすことなく、通常的に使用することができるようになる。  As described above, according to the present invention, fermented milk having a very low redox potential under normal temperature and normal pressure can be obtained, so that it can be used normally without causing any health problems.

Claims (5)

常圧下で酸化還元電位が−10mv以下−2000mv以上である発酵乳。  Fermented milk having a redox potential of −10 mv or less and −2000 mv or more under normal pressure. 0℃〜100℃の発酵乳に−180℃〜90℃の水素ガスを0.1気圧〜1000気圧に加圧して溶解せしめ、常温常圧に戻すことにより得られた発酵乳。  Fermented milk obtained by dissolving hydrogen gas of −180 ° C. to 90 ° C. under pressure of 0.1 to 1000 atm in fermented milk at 0 to 100 ° C. and returning to normal temperature and pressure. 前記発酵乳が水道水、浄化水道水、アルカリイオン水、ミネラル含有水、わき水、海水脱塩水、精製水、純水から選択された少なくとも1つを含んでいることを特徴とする請求項2に記載の発酵乳。  The fermented milk contains at least one selected from tap water, purified tap water, alkali ion water, mineral-containing water, side water, seawater desalted water, purified water, and pure water. The fermented milk described. 以下の(1)及び(2)の行程からなる発酵乳の製造方法。
(1)0℃〜100℃の発酵乳に−180℃〜90℃の水素ガスを0.1気圧〜1000気圧に加圧して溶解せしめる行程。
(2)前記(1)の行程で得られた発酵乳を常圧に戻す行程。
A method for producing fermented milk comprising the following steps (1) and (2).
(1) A process in which hydrogen gas at −180 ° C. to 90 ° C. is pressurized to 0.1 atm to 1000 atm in fermented milk at 0 ° C. to 100 ° C.
(2) The process which returns fermented milk obtained by the process of said (1) to a normal pressure.
前記水素ガスをバッチ式又は連続流通式に供給することを特徴とする請求項4に記載の発酵乳の製造方法。  The method for producing fermented milk according to claim 4, wherein the hydrogen gas is supplied batchwise or continuously.
JP2003363838A 2003-09-18 2003-09-18 Reducing fermented milk and method for producing the same Pending JP2005087193A (en)

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