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JP2015033360A - Hydrogen-containing beverage containing functional raw material - Google Patents

Hydrogen-containing beverage containing functional raw material Download PDF

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JP2015033360A
JP2015033360A JP2013166473A JP2013166473A JP2015033360A JP 2015033360 A JP2015033360 A JP 2015033360A JP 2013166473 A JP2013166473 A JP 2013166473A JP 2013166473 A JP2013166473 A JP 2013166473A JP 2015033360 A JP2015033360 A JP 2015033360A
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hydrogen
water
raw material
gas
containing beverage
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五十嵐 純一
Junichi Igarashi
純一 五十嵐
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SHEFCO CO Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a hydrogen-containing beverage containing a functional raw material such as the extract of cherry blossoms and hydrogen water, in which high dissolved hydrogen concentration is held.SOLUTION: Provided is a hydrogen-containing beverage in which a functional raw material selected from the group consisting of the extract of cherry blossoms, apple polyphenol, the extract of kiwi seeds, methyl hesperidin theanine, polyamine, polydextrol and the extract of loose blossoms is blended into hydrogen water dissolved with a hydrogen gas.

Description

本発明は、機能性原料を含有する水素含有飲料に関する。   The present invention relates to a hydrogen-containing beverage containing a functional raw material.

近年、半導体用シリコン基板や液晶用ガラス基板などの洗浄にも用いられている(超)純水に水素ガスを溶解させた水素溶解水(単に水素水ともいう)は、高い還元性を有することから、金属の酸化や食品類の腐敗を抑制する効果があるとされ、また飲用へ転用した場合には様々な健康障害の改善を期待できるとして注目されている。   In recent years, hydrogen-dissolved water in which hydrogen gas is dissolved in (ultra) pure water (also simply referred to as hydrogen water), which is also used for cleaning semiconductor silicon substrates and glass substrates for liquid crystals, has high reducibility Therefore, it is said that it has the effect of suppressing metal oxidation and food spoilage, and when it is diverted to drinking, it is attracting attention as being expected to improve various health disorders.

上述の飲用向けの水素溶解水を製造する方法としては、例えばガスボンベからの水素ガス、或いは水の電気分解により発生した水素ガスを原水に溶解させる方法がある。ただし、単に水素ガスを原水中に供給するだけでは、室温・大気圧下では原水中に溶存している窒素ガス、酸素ガスなどが水素ガスの溶解を邪魔するため、その溶存水素濃度は水素の飽和濃度に遠く及ばない。
このため、例えば空気を除去した圧力容器内に水素ガスを充填し、該圧力容器内における水素ガスの圧力を2〜10気圧に保ったまま、その圧力容器内に原水をシャワー状に散水して水素ガスと接触させることにより、水素ガスを効率よく溶解させる方法が提案されている(特許文献1)。
あるいは、水に高圧で水素ガスを噴射して超微細気泡(所謂“ナノバブル”“マイクロバブル”)を発生させ、これを水に溶解させる方法が提案されている(特許文献2)。
As a method for producing the above-described drinking hydrogen-dissolved water, for example, there is a method in which hydrogen gas from a gas cylinder or hydrogen gas generated by electrolysis of water is dissolved in raw water. However, simply supplying hydrogen gas to the raw water causes nitrogen gas, oxygen gas, etc. dissolved in the raw water to interfere with the dissolution of hydrogen gas at room temperature and atmospheric pressure. It is far from the saturated concentration.
For this reason, for example, hydrogen gas is filled in a pressure vessel from which air has been removed, and the raw water is sprayed into the pressure vessel in a shower-like manner while maintaining the hydrogen gas pressure in the pressure vessel at 2 to 10 atm. A method for efficiently dissolving hydrogen gas by bringing it into contact with hydrogen gas has been proposed (Patent Document 1).
Alternatively, a method has been proposed in which hydrogen gas is injected into water at high pressure to generate ultrafine bubbles (so-called “nanobubbles” and “microbubbles”), which are dissolved in water (Patent Document 2).

ところで、上述の水素水のように、水素ガスを溶解させた飲料が有する高い還元性に注目して、お茶やコーヒー、清涼飲料水、あるいは野菜ジュース等に水素を溶解させることにより、酸化還元電位が低い飲料に関する種々の提案もなされている(特許文献3乃至特許文献5)。
また水素を溶解させた飲料は、製造から実際に飲用するまでに溶存水素量の損失が少なく高い還元性が維持されることが重要であり、還元性の持続性を高めるとして抗酸化物質(還元性物質)を添加することが提案されている(特許文献6及び特許文献7)。
By the way, paying attention to the high reducibility of beverages in which hydrogen gas is dissolved, such as the hydrogen water described above, redox potential can be obtained by dissolving hydrogen in tea, coffee, soft drinks, vegetable juice, etc. Various proposals relating to beverages with a low content have also been made (Patent Documents 3 to 5).
In addition, it is important for beverages in which hydrogen is dissolved to maintain high reducibility with little loss of dissolved hydrogen from production to actual consumption. It has been proposed to add an active substance) (Patent Documents 6 and 7).

特許第3606466号公報Japanese Patent No. 3606466 特開2011−230055号公報JP 2011-230055 A 特開2004−329188号公報JP 2004-329188 A 特開2004−344862号公報JP 2004-344862 A 特開2005−21146号公報JP 2005-21146 A 特開2005−296794号公報JP 2005-296794 A 国際公開第2008−062814号パンフレットInternational Publication No. 2008-062814 Pamphlet

しかしながら、従来提案された水素含有飲料は、原料水(液体)に水素ガスを効率よく溶解できず、またロット毎に水素濃度にばらつきが生ずるという問題があった。
また抗酸化物質(還元性物質)を添加することにより高い還元性の維持を図った飲料であっても、従来の製法で得られた水素含有水(水素含有飲料)はそれ自体の水素濃度が低く、所望の酸化還元電位を有する飲料を提供できないという問題があった。
さらに、高い溶存濃度水素濃度を有する水素含有飲料を製造できても、保管中に溶存水
素濃度が大きく低下してしまうという問題があった。
However, conventionally proposed hydrogen-containing beverages have a problem that hydrogen gas cannot be efficiently dissolved in the raw water (liquid) and the hydrogen concentration varies from lot to lot.
In addition, even in beverages that maintain high reducibility by adding antioxidant substances (reducing substances), hydrogen-containing water (hydrogen-containing drinks) obtained by conventional methods has its own hydrogen concentration. There was a problem that it was low and could not provide a beverage having a desired redox potential.
Furthermore, even if a hydrogen-containing beverage having a high dissolved concentration hydrogen concentration can be produced, there has been a problem that the dissolved hydrogen concentration is greatly reduced during storage.

本発明者らは上記の課題を解決する為に水素含有水に添加し得る天然成分や飲用材料について鋭意検討を重ねた結果、桜の花抽出物類等の特定の機能性原料を水素水に好ましい量にて配合し水素含有飲料とすることにより、得られた水素含有飲料において長期間高い溶存水素濃度を維持できること、且つ得られた水素含有飲料が無着色、無臭、無味の材料となりその他の飲料成分の自由な配合が可能となることを見出し、さらに使用する水素水として、原料となる水から残存ガスを脱気し、これにガス透過性中空糸膜を介して水素ガスを溶解させることにより溶存水素濃度をより効率的に高めた水素水を用いることにより、高い溶存水素濃度を維持した水素含有飲料となることを見出し、本発明を完成させた。   As a result of intensive studies on natural ingredients and drinkable materials that can be added to hydrogen-containing water in order to solve the above-mentioned problems, the present inventors preferred specific functional raw materials such as cherry blossom extracts for hydrogen water. By blending in an amount to make a hydrogen-containing beverage, the resulting hydrogen-containing beverage can maintain a high dissolved hydrogen concentration for a long period of time, and the resulting hydrogen-containing beverage becomes a non-colored, odorless, tasteless material and other beverage By finding that the components can be freely blended, and by degassing the remaining gas from the raw water as the hydrogen water to be used, and dissolving the hydrogen gas through this gas-permeable hollow fiber membrane The present inventors have found that a hydrogen-containing beverage maintaining a high dissolved hydrogen concentration can be obtained by using hydrogen water having a higher dissolved hydrogen concentration more efficiently, and the present invention has been completed.

すなわち、本発明は、カフェオイルグルコース、ケルセチングルコシド、クマロイルグルコース、シンナモイルグルコース、ケンフェロールグルコシド、ケルセチンマロニルグルコース及びケンフェロールマロニルグルコースからなる群から選択される少なくとも一種を含有する桜の花抽出物;プロシアニジン及びケルセチンのうち少なくとも一種を含有するリンゴポリフェノール;クエルシトリン及びケンペロール3−O−ラムノシドのうち少なくとも一種を含有するキウイ種子抽出物;メチルヘスペリジン;テアニン;スペルミジン、スペルミン及びプトレスシンのうち少なくとも一種を含有するポリアミン;ポリデキストロース;並びにオイゲニインを含有するバラの花抽出物からなる群から選択される少なくとも一種の機能性原料が、水素ガスが溶解された水素水に配合された水素含有飲料に関する。   That is, the present invention is a cherry blossom flower extract containing at least one selected from the group consisting of caffeoyl glucose, quercetin glucoside, coumaroyl glucose, cinnamoyl glucose, kaempferol glucoside, quercetin malonyl glucose and kaempferol malonyl glucose; Apple polyphenol containing at least one of procyanidins and quercetin; Kiwi seed extract containing at least one of quercitrin and kaempferol 3-O-rhamnoside; methyl hesperidin; theanine; containing at least one of spermidine, spermine and putrescine At least one functional raw material selected from the group consisting of polydextrose; polydextrose; and rose flower extract containing eugenin It relates to a hydrogen-containing beverage in which the hydrogen gas is blended to hydrogen water dissolved.

前記水素含有飲料は、原料となる水を脱気し、これにガス透過性中空糸膜を介して水素ガスを溶解することにより水素水を製造し、そして製造された水素水に前記機能性原料を溶解又は混合することにより調製されてなるか、或いは、原料となる水に前記機能性原料を溶解又は混合し、これを脱気し、そしてこれにガス透過性中空糸膜を介して水素ガスを溶解することにより調製されてなることが好ましい。   The hydrogen-containing beverage is produced by degassing water as a raw material and dissolving hydrogen gas in the hydrogen-containing beverage through a gas-permeable hollow fiber membrane, and the functional raw material is added to the produced hydrogen water. Or the functional raw material is dissolved or mixed in water as a raw material, degassed, and hydrogen gas is passed through a gas-permeable hollow fiber membrane. It is preferable to be prepared by dissolving

より好ましくは、前述の水素含有飲料が殺菌・滅菌されていることが好ましい。また、脱気の前に、原料となる水又はこれに機能性原料が混合又は溶解された水は、ろ過及び/又は浄化されてなることが好ましい。   More preferably, the aforementioned hydrogen-containing beverage is preferably sterilized and sterilized. Moreover, it is preferable to filter and / or purify the water used as a raw material or the water in which a functional raw material is mixed or dissolved before degassing.

一般に、本発明の水素含有飲料は、前記機能性原料を該水素含有飲料の総質量に対して0.001質量%〜20質量%の割合で含有することが好ましい。尤もそれぞれの機能性原料の添加量は、水素含有飲料が無着色、無臭、無味の性質を有効に維持し得る範囲で、なるべく高い溶存水素濃度を長期間維持し得る範囲の量に設定される。   Generally, the hydrogen-containing beverage of the present invention preferably contains the functional raw material in a proportion of 0.001% by mass to 20% by mass with respect to the total mass of the hydrogen-containing beverage. However, the amount of each functional ingredient added is set in such a range that the hydrogen-containing beverage can maintain the non-colored, odorless, and tasteless properties effectively, and can maintain a high dissolved hydrogen concentration as long as possible. .

本発明によれば、桜の花抽出物類等の機能性原料を水素水に配合することにより、得られた水素含有飲料において長期間高い溶存水素濃度を維持することができる。
また、機能性原料として食品や食品衛生法等で認められている食品添加物を使用しているため、人体に悪影響を与えることがなく、またこれら機能性原料を水素ガスを高濃度で溶解させた水素水に配合することにより、酸化還元電位を低い値に維持した水素含有飲料を得られる。
According to the present invention, a high concentration of dissolved hydrogen can be maintained for a long period of time in the obtained hydrogen-containing beverage by blending functional raw materials such as cherry blossom extract into hydrogen water.
In addition, because it uses food additives approved by the Food and Food Sanitation Law as functional raw materials, it does not adversely affect the human body, and these functional raw materials are dissolved in hydrogen gas at a high concentration. By blending with hydrogen water, a hydrogen-containing beverage having a low oxidation-reduction potential can be obtained.

本発明の水素含有飲料は、桜の花抽出物、リンゴポリフェノール、キウイ種子抽出物、メチルヘスペリジン、テアニン、ポリアミン、ポリデキストロール、バラの花抽出物からなる群から選択される機能性原料が水素水に配合された飲料である。
以下、詳細に説明する。
In the hydrogen-containing beverage of the present invention, the functional raw material selected from the group consisting of cherry blossom extract, apple polyphenol, kiwi seed extract, methyl hesperidin, theanine, polyamine, polydextrol, rose flower extract is hydrogen water. It is a drink blended in.
Details will be described below.

本発明の水素含有飲料に配合する機能性原料としては、例えば以下のものを挙げることができる。
a)桜の花抽出物:カフェオイルグルコース、ケルセチングルコシド、クマロイルグルコース、シンナモイルグルコース、ケンフェロールグルコシド、ケルセチンマロニルグルコース、ケンフェロールマロニルグルコース
b)リンゴポリフェノール:プロシアニジン、ケルセチン
c)キウイ種子抽出物:クエルシトリン、ケンペロール3−O−ラムノシド
d)メチルヘスペリジン
e)テアニン
f)ポリアミン:スペルミジン、スペルミン、プトレスシン
g)ポリデキストロース(数平均分子量:約1500〜約18,000、例えば1500や2000程度)
h)バラの花抽出物:オイゲニイン
As a functional raw material mix | blended with the hydrogen-containing drink of this invention, the following can be mentioned, for example.
a) Cherry blossom extract: caffeoyl glucose, quercetin glucoside, coumaroyl glucose, cinnamoyl glucose, kaempferol glucoside, quercetin malonyl glucose, kaempferol malonyl glucose b) apple polyphenol: procyanidin, quercetin c) kiwi seed extract: quell Citrine, kaempferol 3-O-rhamnoside d) methyl hesperidin e) theanine f) polyamine: spermidine, spermine, putrescine g) polydextrose (number average molecular weight: about 1500 to about 18,000, for example, about 1500 or 2000)
h) Rose flower extract: Eugenin

これら機能性原料は1種単独で、或いは上記a)〜h)における同じ分類中の2種以上、又は異なる分類の2種以上を組み合わせて、本発明の水素含有飲料に配合することができる。
例えば上記a)〜h)における異なる分類の機能性原料を2種以上組み合わせる場合、一例として以下の組み合わせを挙げることができる。なお、本項で“桜の花抽出物”とは前記<a)桜の花抽出物>を、“リンゴポリフェノール”とは上記<b)リンゴポリフェノール>を、“キウイ種子抽出物”とは上記<c)キウイ種子抽出物>を、“ポリアミン”とは上記<f)ポリアミン>を、“バラの花抽出物”とは上記<h)バラの花抽出物>をそれぞれ示し、これらは一種又は二種以上を含んでいても良い。
・桜の花抽出物+ポリアミン及び/又はポリデキストロース
・リンゴポリフェノール+ポリアミン及び/又はポリデキストロース
・キウイ種子抽出物+ポリアミン及び/又はポリデキストロース
・メチルヘスペリジン+ポリアミン及び/又はポリデキストロース
・テアニン+ポリアミン及び/又はポリデキストロース
・バラの花抽出物+ポリアミン及び/又はポリデキストロース
これらの他、無論、桜の花抽出物のみ(例:カフェオイルグルコースとケルセチングルコシドなど)、リンゴポリフェノールのみ(プロシアニジンとケルセチン)などの様々な組み合わせであってもよい。
These functional raw materials can be blended in the hydrogen-containing beverage of the present invention singly or in combination of two or more of the same classifications in a) to h) or two or more of different classifications.
For example, when combining 2 or more types of functional raw materials of different classifications in the above a) to h), the following combinations can be given as an example. In this section, “cherry blossom extract” means <a) cherry blossom extract>, “apple polyphenol” means <b) apple polyphenol>, and “kiwi seed extract” means <c ) Kiwi Seed Extract>, “Polyamine” indicates <f) Polyamine> and “Rose Flower Extract” indicates <h) Rose Flower Extract>, which are one or two of them. The above may be included.
Cherry blossom extract + polyamine and / or polydextrose apple polyphenol + polyamine and / or polydextrose kiwi seed extract + polyamine and / or polydextrose methyl hesperidin + polyamine and / or polydextrose theanine + polyamine and / or Or polydextrose rose flower extract + polyamine and / or polydextrose Other than these, of course, cherry blossom extract only (eg caffeoyl glucose and quercetin glucoside), apple polyphenol only (procyanidin and quercetin) It may be a combination.

またこれら機能性原料(2種以上を配合する場合にはその合計量)は、水素含有飲料の総質量に対して0.001質量%乃至20質量%の割合で配合することができ、好ましくは0.002質量%乃10質量%の割合で、特に0.005質量%乃至5質量%、0.01質量%乃至1質量%、例えば0.025質量%、0.05質量%、0.5質量%程度配合することが好ましい。   Moreover, these functional raw materials (the total amount when two or more types are blended) can be blended in a proportion of 0.001% by mass to 20% by mass with respect to the total mass of the hydrogen-containing beverage, preferably 0.002% to 10% by weight, in particular 0.005% to 5%, 0.01% to 1%, for example 0.025%, 0.05%, 0.5% It is preferable to blend about mass%.

本発明の水素含有飲料は、原料となる水を脱気し、これにガス透過性中空糸膜を介して水素ガスを溶解することにより水素水を製造し、そして製造された水素水に前記機能性原料を溶解又は混合することにより調製されてなる。
あるいは本発明の水素含有飲料は、原料となる水に前記機能性原料を溶解又は混合し、これを脱気し、そしてこれにガス透過性中空糸膜を介して水素ガスを溶解することにより調製されてなる。
なお、機能性原料の液体(例えば野菜ジュース、牛乳など)自体を脱気し、ガス透過性中空糸膜を介して水素ガスを溶解することにより水素含有飲料とすることもできる。
The hydrogen-containing beverage of the present invention produces hydrogen water by degassing water as a raw material and dissolving hydrogen gas through the gas-permeable hollow fiber membrane, and the function is added to the produced hydrogen water. It is prepared by dissolving or mixing the raw material.
Alternatively, the hydrogen-containing beverage of the present invention is prepared by dissolving or mixing the functional raw material in water as the raw material, degassing it, and dissolving hydrogen gas through the gas-permeable hollow fiber membrane. Being done.
In addition, it is also possible to make a hydrogen-containing beverage by degassing the functional raw material liquid (eg, vegetable juice, milk, etc.) itself and dissolving the hydrogen gas through the gas-permeable hollow fiber membrane.

上述の如く調整された水素含有飲料は、飲料として提供するために通常実施される殺菌・滅菌をされ得、また、原料となる水又はこれに機能性原料が混合又は溶解された水から不純物を除去すべく、脱気の前にろ過・又は浄化することもできる。   The hydrogen-containing beverage prepared as described above can be sterilized and sterilized normally for serving as a beverage, and impurities can be removed from the raw water or the water in which the functional raw material is mixed or dissolved. It can also be filtered and / or purified before degassing to eliminate.

原料となる水又はこれに機能性原料が混合又は溶解された水に水素を溶解する方法は、例えば本発明者らが先の特許出願(特願2009−123310号明細書)において開示された方法に準じて、所謂膜溶解法により実施され得、同出願のすべての内容は参照することにより本書に組み込まれる。
上記方法は、具体的には(a)浄化工程、(b)脱気工程、(c)水素溶解工程、(d)殺菌工程を含みて構成され、各工程を閉じられた系において連続して為すことを特徴とする。
The method of dissolving hydrogen in water as a raw material or water in which a functional raw material is mixed or dissolved is, for example, a method disclosed by the present inventors in a previous patent application (Japanese Patent Application No. 2009-123310). The content of the same application is hereby incorporated by reference.
Specifically, the method includes (a) a purification step, (b) a deaeration step, (c) a hydrogen dissolution step, and (d) a sterilization step, and each step is continuously performed in a closed system. It is characterized by doing.

(a)浄化工程
本工程は、浄化装置において原料となる水をろ過し、得られた浄化水を脱気装置に送る工程である。なお本発明においては、原料となる水に前記機能性原料を溶解した水をろ過し、脱気装置に送る工程としても良い。
原料となる水は、飲用に適した水源から供給されたものであれば特に制限は無く、水道水(水道事業の用に供する水道、専用水道若しくは簡易専用水道により供給される水)や地下水等を挙げることができる。
前記浄化装置は、活性炭ろ過装置と膜ろ過装置を備えてなる。
前記活性炭ろ過装置により原料となる水のカビ臭、トリハロメタンの除去や、脱塩素処理などを行う。また安全フィルタろ過装置によって、浮遊物(活性炭などを含む)や、大腸菌などの細菌、クリプトスポリジウムなどの病原性原虫などを除去する。
膜ろ過装置に使用可能な膜としては、精密ろ過膜(MF膜)、限外ろ過膜(UF膜)、ナノフィルター膜(NF膜)、逆浸透膜(RO膜)が挙げられるが、操作性や、飲用とした場合に味の決め手となるミネラル成分の残存性を考慮すると、MF膜を用いることが望ましい。NF膜やRO膜を用いて膜透過処理をすることもできるが、ナトリウムイオンやカリウムイオン等の原水に溶存するミネラル成分まで除去されるため、飲用に適した水とするにはこれらミネラル成分の残存率を調整したり、あるいは新たに添加する必要がでてくることから、操作が煩雑になり好ましくない。
(A) Purification step This step is a step of filtering water that is a raw material in the purification device and sending the obtained purified water to a deaeration device. In the present invention, it is also possible to filter the water in which the functional raw material is dissolved in the raw water and send it to the deaerator.
The water used as a raw material is not particularly limited as long as it is supplied from a water source suitable for drinking, such as tap water (water supplied for water supply business, water supplied by a dedicated water supply or simplified dedicated water supply), groundwater, etc. Can be mentioned.
The purification device includes an activated carbon filtration device and a membrane filtration device.
The activated carbon filter removes the musty odor of water, trihalomethane, and dechlorination treatment. In addition, it removes suspended solids (including activated carbon), bacteria such as Escherichia coli, and pathogenic protozoa such as Cryptosporidium by a safety filter.
Examples of membranes that can be used in membrane filtration devices include microfiltration membranes (MF membranes), ultrafiltration membranes (UF membranes), nanofilter membranes (NF membranes), and reverse osmosis membranes (RO membranes). In view of the remaining of mineral components that determine the taste when drinking, it is desirable to use an MF membrane. Membrane permeation treatment can also be performed using NF membrane or RO membrane, but since mineral components dissolved in raw water such as sodium ions and potassium ions are removed, these mineral components are used to make water suitable for drinking. Since the residual ratio needs to be adjusted or newly added, the operation becomes complicated, which is not preferable.

(b)脱気工程
本工程は、脱気装置に供給された浄化水を脱気し、得られた脱気水を水素溶解装置に送る工程である。
前記脱気装置は、酸素ガス、窒素ガス、炭酸ガス等の溶存気体の脱気を行うことができれば特に制限されず、例えば真空脱気装置や、ガス透過膜内蔵モジュール(ガス脱気膜モジュール)を備えた脱気装置を用いることができるが、微量に溶存する気体を効率よく脱気することができるため、ガス脱気膜モジュールを備えた脱気装置を用いることが好ましい。
該ガス脱気膜モジュールは、ガス脱気膜によって水室と気体室とに区画され、水室に前記浄化水を通過させ、気体室を減圧することにより、水室に流れる溶存気体を脱気する。
本工程で用いるガス脱気膜(中空糸膜)の種類は特に制限は無く、例えば、ポリプロピレン、ポリジメチルシロキサン、ポリカーボネート−ポリジメチルシロキサンブロック共重合体、ポリビニルフェノール−ポリジメチルシロキサン−ポリスルホンブロック共重合体、ポリ(4−メチルペンテン−1−)、ポリ(2,6−ジメチルフェニレンオキシド)、ポリテトラフルオロエチレン等の高分子膜を挙げることができる。
なお、脱気効率を高めるために本工程を加温下で実施してもよく、その場合には、その後の水素溶解の効率を上げるために、室温(25℃前後)まで冷却することが望ましい。
(B) Degassing step This step is a step of degassing the purified water supplied to the degassing device and sending the obtained degassed water to the hydrogen dissolving device.
The degassing device is not particularly limited as long as it can degas a dissolved gas such as oxygen gas, nitrogen gas, and carbon dioxide gas. For example, a vacuum degassing device or a gas permeable membrane built-in module (gas degassing membrane module) However, since a gas dissolved in a small amount can be efficiently degassed, it is preferable to use a degasser equipped with a gas degassing membrane module.
The gas degassing membrane module is partitioned into a water chamber and a gas chamber by a gas degassing membrane, passes the purified water through the water chamber, and depressurizes the gas chamber, thereby degassing the dissolved gas flowing into the water chamber. To do.
The type of gas degassing membrane (hollow fiber membrane) used in this step is not particularly limited. For example, polypropylene, polydimethylsiloxane, polycarbonate-polydimethylsiloxane block copolymer, polyvinylphenol-polydimethylsiloxane-polysulfone block copolymer Examples thereof include polymer films such as coalescence, poly (4-methylpentene-1-), poly (2,6-dimethylphenylene oxide), and polytetrafluoroethylene.
In order to increase the efficiency of deaeration, this step may be performed under heating. In that case, in order to increase the efficiency of subsequent hydrogen dissolution, it is desirable to cool to room temperature (around 25 ° C.). .

(c)水素溶解工程
本工程は、水素溶解装置に供給された脱気水に水素ガスを溶解させ、得られた水素溶解水を殺菌装置に送る工程である。
前記水素溶解装置としては、単位時間、単位スペース辺りの水素ガス溶解量が大きく、水素ガスの溶解効率を高めることが容易であることから、ガス透過膜モジュールを備えた水素溶解装置を用いる。
前記ガス透過膜モジュールは、ガス透過膜によって水室と気体室とに区画され、水室に前記脱気水を通過させ、気体室に水素ガスを供給することにより、水室に流れる脱気水に水素ガスを溶解させる。
本工程で使用するガス透過膜としては、前述のガス脱気膜として挙げた高分子膜を挙げることができる。
(C) Hydrogen dissolution step This step is a step of dissolving hydrogen gas in deaerated water supplied to the hydrogen dissolution apparatus and sending the obtained hydrogen dissolution water to the sterilization apparatus.
As the hydrogen dissolving apparatus, a hydrogen dissolving apparatus equipped with a gas permeable membrane module is used because the amount of hydrogen gas dissolved per unit time and unit space is large and it is easy to improve the dissolution efficiency of hydrogen gas.
The gas permeable membrane module is divided into a water chamber and a gas chamber by a gas permeable membrane, passes the degassed water through the water chamber, and supplies hydrogen gas to the gas chamber, thereby supplying degassed water flowing into the water chamber. Hydrogen gas is dissolved in
Examples of the gas permeable membrane used in this step include the polymer membranes mentioned as the gas degassing membrane.

水素ガスの供給方法には特に制限は無く、例えば市販の高純度水素ガスボンベや水の電気分解などで得られる水素ガスを使用することができる。
また水素ガスを該ガス透過膜モジュールの気体室に供給する際、水素ガスを大気圧以上、例えば1.2気圧〜2.0気圧程度の圧力をかけて供給することにより、溶存水素濃度を高めることができる。ただし2.0気圧を超える圧力をかけると、ガス透過膜モジュールの各種設備の耐圧性や気密性を高める必要があり、製造コストの増加につながるため好ましくない。
There is no restriction | limiting in particular in the supply method of hydrogen gas, For example, the hydrogen gas obtained by the electrolysis etc. of a commercially available high purity hydrogen gas cylinder or water can be used.
Further, when supplying hydrogen gas to the gas chamber of the gas permeable membrane module, the dissolved hydrogen concentration is increased by supplying hydrogen gas at a pressure higher than atmospheric pressure, for example, about 1.2 to 2.0 atm. be able to. However, if a pressure exceeding 2.0 atm is applied, it is necessary to improve the pressure resistance and airtightness of various facilities of the gas permeable membrane module, which leads to an increase in manufacturing cost, which is not preferable.

(d)殺菌工程
本工程は、殺菌装置に供給された水素溶解水を殺菌する殺菌工程である。
前記殺菌装置は、紫外線照射装置と膜ろ過装置を備えてなり、前記紫外線照射装置により水素溶解水を殺菌し、膜ろ過装置により浮遊物や細菌等を再度除去する。
本工程においても、前記浄化装置と同様にMF膜ろ過装置を用いることが好ましいが、前記浄化装置で用いたMF膜よりも孔径の小さいMF膜を用いることにより、前記浮遊物等を完全に除去することができるのでより望ましい。
(D) Sterilization process This process is a sterilization process of sterilizing the hydrogen-dissolved water supplied to the sterilizer.
The sterilizer includes an ultraviolet irradiation device and a membrane filtration device, sterilizes hydrogen-dissolved water with the ultraviolet irradiation device, and again removes suspended matters, bacteria, and the like with the membrane filtration device.
Also in this step, it is preferable to use an MF membrane filtration device as in the purification device, but the suspended matter and the like are completely removed by using an MF membrane having a pore diameter smaller than that of the MF membrane used in the purification device. It is more desirable because it can.

なお工程(d)で得られた水素水の一部を工程(b)の脱気装置に戻し、工程(b)乃至工程(d)の間で水循環させ、特に水循環中には前記脱気装置への浄化水の供給を一時停止することにより、より効率的に水素ガスを脱気水に溶解させることができ、水素ガス溶存濃度の高い水素水を製造できる。具体的には、室温・大気圧下で通常1.6ppm程度とされる水素溶存濃度を約2倍にまで高めることができる。   A part of the hydrogen water obtained in the step (d) is returned to the degassing device in the step (b), and water is circulated between the steps (b) to (d). By temporarily stopping the supply of purified water to the hydrogen gas, hydrogen gas can be more efficiently dissolved in the deaerated water, and hydrogen water having a high concentration of dissolved hydrogen gas can be produced. Specifically, the hydrogen-dissolved concentration, which is usually about 1.6 ppm at room temperature and atmospheric pressure, can be increased to about twice.

こうして製造された水素水は、前述の機能性原料と混合させることにより、本発明の水素含有飲料を得る。また原料となる水に既に機能性原料を溶解している場合には、工程(d)を経ることにより本発明の水素含有飲料を得られる。
なお、機能性原料を含有する水素含有飲料は、製造後に密封容器に充填し、所望により加熱殺菌を行う。
前記密封容器としては特に限定されず、ラミネートフィルムなどで作られた袋状容器や金属缶等を挙げることができ、特にアルミラミネートフィルム製の袋状容器が気密性が高く水素の流出を防ぐことができるため好ましい。該袋状容器にはプラスチック製の吸い口(スパウト)などが設けられていてもよい。そして前記密封容器の種類に応じた充填装置を用いて、水素含有水を密封容器に充填し、密封する。
また密封容器に充填した水素含有飲料は、例えば加熱蒸気殺菌装置を用いて、85〜90℃、20分〜1時間の間で水製品を加熱殺菌し得る。
The hydrogen water produced in this way is mixed with the aforementioned functional raw material to obtain the hydrogen-containing beverage of the present invention. Moreover, when the functional raw material is already melt | dissolved in the water used as a raw material, the hydrogen containing drink of this invention can be obtained by passing through a process (d).
In addition, the hydrogen-containing drink containing a functional raw material is filled in a sealed container after production, and is heat-sterilized as desired.
The sealed container is not particularly limited, and examples thereof include a bag-like container made of a laminate film, a metal can, and the like. Particularly, a bag-like container made of an aluminum laminate film is highly airtight and prevents hydrogen from flowing out. Is preferable. The bag-like container may be provided with a plastic mouthpiece (spout) or the like. And using the filling apparatus according to the kind of the said sealed container, hydrogen containing water is filled into a sealed container, and it seals.
Moreover, the hydrogen-containing drink with which the sealed container was filled can heat-sterilize a water product between 85-90 degreeC and 20 minutes-1 hour, for example using a heating steam sterilizer.

本発明の望ましい実施形態をさらに具体的に説明するが、これによって本発明が限定されるものではない。   Preferred embodiments of the present invention will be described more specifically, but the present invention is not limited thereto.

[参考例1:水素溶存方法の違いによる酸化還元電位の安定性評価]
以下の1)〜3)の水素溶存方法を用いて水素水を製造し、酸化還元電位の経時変化を測定した。水素溶存方法は以下のとおりである。
1)膜溶解法:本試験で使用した水素水は、本発明者らが先の特許出願(特願2009−123310号明細書)において開示された方法により、好適に製造できる。
すなわち、(1)浄化装置において原料となる水をろ過及び浄化し、得られた浄化水を脱気装置に送る浄化工程と、(2)前記脱気装置に供給された浄化水を脱気し、得られた脱気水を水素溶解装置に送る脱気工程と、(3)前記水素溶解装置に供給された脱気水に水素ガスを溶解させ、得られた水素溶解水を殺菌装置に送る水素溶解工程と、(4)前記殺菌装置に供給された水素溶解水を殺菌する方法により、水素水を製造した。
2)加圧式:缶体に水と水素ガスを導入して、缶体内を加圧して水素ガスを溶解させた。ただし水素ガスの導入前に、水の脱気処理は行わなかった。
3)マイクロバブリング法:水素ガスを微細な泡にして、水に導入して水素ガスを溶解させた。ただし水素ガスの導入前に、水の脱気処理は行わなかった。
[Reference Example 1: Evaluation of stability of oxidation-reduction potential due to difference in hydrogen dissolution method]
Hydrogen water was produced using the following hydrogen dissolution methods 1) to 3), and the change with time of the oxidation-reduction potential was measured. The hydrogen dissolution method is as follows.
1) Membrane dissolution method: The hydrogen water used in this test can be suitably produced by the method disclosed by the present inventors in a previous patent application (Japanese Patent Application No. 2009-123310).
That is, (1) a purification step of filtering and purifying water as a raw material in the purification device and sending the obtained purified water to the deaeration device; and (2) degassing the purification water supplied to the deaeration device. A degassing step of sending the obtained degassed water to the hydrogen dissolving device; (3) dissolving hydrogen gas in the degassed water supplied to the hydrogen dissolving device, and sending the obtained hydrogen dissolved water to the sterilizer Hydrogen water was produced by a hydrogen dissolution step and (4) a method of sterilizing the hydrogen-dissolved water supplied to the sterilizer.
2) Pressurization type: Water and hydrogen gas were introduced into the can, and the can was pressurized to dissolve the hydrogen gas. However, water was not deaerated before the introduction of hydrogen gas.
3) Micro bubbling method: Hydrogen gas was made into fine bubbles and introduced into water to dissolve the hydrogen gas. However, water was not deaerated before the introduction of hydrogen gas.

酸化還元電位の測定は以下の手順にて行った。
まず、各方法で製造した水素水をそれぞれ200mLを量りとり、各方法ごとに2サンプルずつ、計6サンプル(例1〜例6)用意した。用意した各サンプルを、2時間経過後を初回測定とし、以後、1時間おきに酸化還元電位とpH値を測定した。6サンプル全ての酸化還元電位がプラス値となった時点で測定を終了し、最後に6サンプル全ての検体の溶存水素濃度を測定した。
得られた結果を表1及び表2に示す。
The redox potential was measured according to the following procedure.
First, 200 mL of hydrogen water produced by each method was weighed, and 2 samples were prepared for each method, for a total of 6 samples (Examples 1 to 6). Each sample prepared was measured for the first time after 2 hours, and thereafter, the oxidation-reduction potential and the pH value were measured every other hour. The measurement was terminated when the oxidation-reduction potentials of all six samples became positive values, and finally the dissolved hydrogen concentrations of the specimens of all six samples were measured.
The obtained results are shown in Tables 1 and 2.

Figure 2015033360
Figure 2015033360

Figure 2015033360
Figure 2015033360

表1及び表2に示すように、膜溶解法を用いて製造した水素水は、加圧法・マイクロバブリング法を用いて製造した水素水と比べ、製造後から最も長く低い酸化還元電位(マイナス値)を維持しており、また、7時間経過後において、最も高い溶損水素濃度を有して
いた。
As shown in Table 1 and Table 2, the hydrogen water produced using the membrane dissolution method is the longest and lower redox potential (minus value) after production compared to the hydrogen water produced using the pressurization method / micro-bubbling method. ) And the highest dissolved hydrogen concentration after 7 hours.

[実施例1:水素含有飲料の製造]
上述の参考例1に示す“膜溶解法”を用いた水素水を使用して水素水を製造した。
得られた水素水を200mL量りとり、これに機能性原料を以下の表3及び表4に示す割合でそれぞれ投入・撹拌・混合し、水素含有飲料とした。
[Example 1: Production of hydrogen-containing beverage]
Hydrogen water was produced using hydrogen water using the “membrane dissolution method” shown in Reference Example 1 above.
200 mL of the obtained hydrogen water was weighed, and functional raw materials were charged, stirred, and mixed at the ratios shown in Tables 3 and 4 below to obtain a hydrogen-containing beverage.

[実施例2:水素含有飲料の還元性評価]
混合後、一定時間経過後の溶存水素濃度、pH及び酸化還元電位を測定した。これらの数値を表3及び表4にあわせて示す。なお、酸化還元電位がマイナスであることが好ましい。
[Example 2: Evaluation of reducibility of hydrogen-containing beverage]
After mixing, the dissolved hydrogen concentration, pH, and oxidation-reduction potential after a certain period of time were measured. These numerical values are shown together in Tables 3 and 4. Note that the redox potential is preferably negative.

Figure 2015033360
Figure 2015033360

Figure 2015033360
Figure 2015033360

上記表3〜表4に示すように、本発明の水素含有飲料は、時間経過後の酸化還元電位が低く保たれるとする結果が得られた。   As shown in Tables 3 to 4, the hydrogen-containing beverage of the present invention has a result that the redox potential after the lapse of time is kept low.

Claims (5)

カフェオイルグルコース、ケルセチングルコシド、クマロイルグルコース、シンナモイルグルコース、ケンフェロールグルコシド、ケルセチンマロニルグルコース及びケンフェロールマロニルグルコースからなる群から選択される少なくとも一種を含有する桜の花抽出物;
プロシアニジン及びケルセチンのうち少なくとも一種を含有するリンゴポリフェノール;クエルシトリン及びケンペロール3−O−ラムノシドのうち少なくとも一種を含有するキウイ種子抽出物;
メチルヘスペリジン;
テアニン;
スペルミジン、スペルミン及びプトレスシンのうち少なくとも一種を含有するポリアミン;
ポリデキストロース;並びに
オイゲニインを含有するバラの花抽出物
からなる群から選択される少なくとも一種の機能性原料が、水素ガスが溶解された水素水に配合された水素含有飲料。
Cherry blossom flower extract containing at least one selected from the group consisting of caffeoyl glucose, quercetin glucoside, coumaroyl glucose, cinnamoyl glucose, kaempferol glucoside, quercetin malonyl glucose and kaempferol malonyl glucose;
Apple polyphenol containing at least one of procyanidins and quercetin; kiwi seed extract containing at least one of quercitrin and kaempferol 3-O-rhamnoside;
Methyl hesperidin;
Theanine;
A polyamine containing at least one of spermidine, spermine and putrescine;
A hydrogen-containing beverage in which at least one functional raw material selected from the group consisting of polydextrose; and rose flower extract containing eugenin is blended in hydrogen water in which hydrogen gas is dissolved.
前記水素含有飲料が、
原料となる水を脱気し、これにガス透過性中空糸膜を介して水素ガスを溶解することにより水素水を製造し、そして製造された水素水に前記機能性原料を溶解又は混合することにより調製されてなるか、或いは、
原料となる水に前記機能性原料を溶解又は混合し、これを脱気し、そしてこれにガス透過性中空糸膜を介して水素ガスを溶解することにより調製されてなる、請求項1に記載の水素含有飲料。
The hydrogen-containing beverage is
Degassing water as a raw material, and dissolving hydrogen gas in this through a gas permeable hollow fiber membrane to produce hydrogen water, and dissolving or mixing the functional raw material in the produced hydrogen water Or prepared by
It is prepared by dissolving or mixing the functional raw material in water as a raw material, degassing it, and dissolving hydrogen gas through this through a gas-permeable hollow fiber membrane. Of hydrogen-containing beverages.
前記水素含有飲料が殺菌・滅菌されている、請求項1又は請求項2に記載の水素含有飲料。 The hydrogen-containing beverage according to claim 1 or 2, wherein the hydrogen-containing beverage is sterilized and sterilized. 脱気の前に、原料となる水又はこれに機能性原料が混合又は溶解された水は、ろ過及び/又は浄化されてなる、請求項2又は請求項3に記載の水素含有飲料。 The hydrogen-containing beverage according to claim 2 or 3, wherein water that is a raw material or water in which a functional raw material is mixed or dissolved is filtered and / or purified before deaeration. 前記機能性原料を該水素含有飲料の総質量に対して0.001質量%〜20質量%の割合で含有する、請求項1乃至請求項4のうち何れか一項に記載の水素含有飲料。 The hydrogen-containing beverage according to any one of claims 1 to 4, wherein the functional raw material is contained in a proportion of 0.001% by mass to 20% by mass with respect to the total mass of the hydrogen-containing beverage.
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