JP5710039B1 - Addition of hydrogen retained in hydrogen storage alloy to liquid - Google Patents

Addition of hydrogen retained in hydrogen storage alloy to liquid Download PDF

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JP5710039B1
JP5710039B1 JP2014045589A JP2014045589A JP5710039B1 JP 5710039 B1 JP5710039 B1 JP 5710039B1 JP 2014045589 A JP2014045589 A JP 2014045589A JP 2014045589 A JP2014045589 A JP 2014045589A JP 5710039 B1 JP5710039 B1 JP 5710039B1
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総 橋本
総 橋本
哲也 宮武
哲也 宮武
理善 西
理善 西
靖世 青山
靖世 青山
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23124Diffusers consisting of flexible porous or perforated material, e.g. fabric
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312Diffusers
    • B01F23/23124Diffusers consisting of flexible porous or perforated material, e.g. fabric
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/236Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages
    • B01F23/2361Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages within small containers, e.g. within bottles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
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    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2376Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
    • B01F23/23764Hydrogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/68Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
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    • C02F1/686Devices for dosing liquid additives
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage

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Abstract

【課題】液体に対して、容器サイズを問わず、簡便な手法で、高濃度の水素を添加する。【解決手段】水素吸蔵合金から取り出した水素を液体に添加する。液体を収容した液体容器100に、水素吸蔵合金を収容した水素吸蔵合金容器20を接続するとともに、水素吸蔵合金を所定温度に加温することで当該容器内の水素ガス圧を高め、当該ガス圧により水素を液体容器内の液体に添加する。ガス圧を調整することで液体に水素を添加するので、ヘンリーの法則に従って、液体容器のサイズとは無関係に、高濃度で水素を添加することが可能になる。なお「液体」とは、代表的には、水、お茶、コーヒー、その他のあらゆる液体、および医療用途として使用される電解質液(生理食塩液、電解質が入った点滴液等)である。【選択図】図1A high-concentration hydrogen is added to a liquid by a simple method regardless of the container size. Hydrogen extracted from a hydrogen storage alloy is added to a liquid. The hydrogen storage alloy container 20 containing the hydrogen storage alloy is connected to the liquid container 100 containing the liquid, and the hydrogen storage alloy is heated to a predetermined temperature to increase the hydrogen gas pressure in the container. To add hydrogen to the liquid in the liquid container. Since hydrogen is added to the liquid by adjusting the gas pressure, it is possible to add hydrogen at a high concentration according to Henry's law regardless of the size of the liquid container. The “liquid” is typically water, tea, coffee, any other liquid, and an electrolyte solution (physiological saline solution, drip solution containing an electrolyte, etc.) used for medical purposes. [Selection] Figure 1

Description

本発明は、液体に対して、容器サイズを問わず、簡便な手法で、高濃度の水素を添加するための工夫に関する。   The present invention relates to a device for adding high-concentration hydrogen to a liquid by a simple method regardless of the container size.

近年、水素水の飲用による健康効果が話題になっている。水素水の飲用により、抗炎症効果や抗酸化作用の他、糖尿病、便秘、歯周病対策、その他多くの健康効果が確認されており、健康志向の高まりとともに飲用者が増えてきている。
なお、水素水の飲用による健康効果は、水素の摂取量と頻度に相関すると考えられている。すなわち、水素水の濃度が2倍になれば、半分量の水素水の飲用で、同等程度の健康効果が期待できる。
In recent years, the health effects of drinking hydrogen water have become a hot topic. In addition to anti-inflammatory and antioxidant effects, many other health effects such as diabetes, constipation, periodontal disease, and other health effects have been confirmed by drinking hydrogen water.
In addition, it is thought that the health effect by drinking hydrogen water correlates with the intake amount and frequency of hydrogen. That is, if the concentration of hydrogen water is doubled, the same level of health effects can be expected by drinking half the amount of hydrogen water.

水素水を製造する装置類として、例えば特許文献1に開示されたものがある。これは、水素発生部で発生させた水素を圧力タンクに導いて水素水を製造する工場設備であって、家庭等で簡便に利用できるものではない。   As an apparatus for producing hydrogen water, for example, there is one disclosed in Patent Document 1. This is a factory facility for producing hydrogen water by introducing hydrogen generated in the hydrogen generation section to a pressure tank and cannot be easily used at home or the like.

一方、水を入れたペットボトル等の容器内に、水素発生材が封入された試験管(スピッツ)を入れて逆止弁付きのキャップを閉め、容器内で水素水を作るものが提案されている(例えば、特許文献2)。しかしながら、スピッツは特定容量のペットボトルに対して専用的に使用するように作られる。例えば、500mlのペットボトルに使用するスピッツは、それに応じた量の水素発生材が封入されており、対象となるペットボトルの容量が異なれば、必要な水素発生材の量も異なる。それ故に、次のような問題が残る。
例えば、500mlのペットボトル専用のスピッツを300mlのペットボトルに使用すると、水素濃度は高くなるが、圧力が過大になりペットボトルの耐圧を超えてしまう。一方、1000mlのペットボトルに使用すると、水素濃度が予定値よりも低くなってしまう。つまり、ペットボトルの容量毎に専用のスピッツを用意する必要があり、汎用性に劣る。
On the other hand, it has been proposed that a test tube (Spitz) filled with a hydrogen generating material is placed in a container such as a plastic bottle containing water, the cap with a check valve is closed, and hydrogen water is produced in the container. (For example, Patent Document 2). However, Spitz is made to be used exclusively for a specific volume of PET bottles. For example, Spitz used for a 500 ml PET bottle contains a hydrogen generating material in an amount corresponding thereto, and the amount of hydrogen generating material required varies depending on the capacity of the target PET bottle. Therefore, the following problems remain.
For example, when Spitz dedicated to a 500 ml PET bottle is used for a 300 ml PET bottle, the hydrogen concentration increases, but the pressure becomes excessive and exceeds the pressure resistance of the PET bottle. On the other hand, when used for a 1000 ml PET bottle, the hydrogen concentration is lower than the expected value. That is, it is necessary to prepare a dedicated spitz for each capacity of the PET bottle, which is inferior in versatility.

なお、特許文献3には、浄水器タイプの水素水製造装置が開示されているが、この装置は、水道水を供給する蛇口に接続して使用することが必須となる。また、水素ガスボンベを使用するが故に、高圧ガス保安法に準拠してガス漏れ検知器を設置する必要がある等、使用に際して制約が多い。   Although Patent Document 3 discloses a water purifier type hydrogen water production apparatus, it is essential that this apparatus is connected to a faucet that supplies tap water. In addition, since a hydrogen gas cylinder is used, there are many restrictions in use, such as the need to install a gas leak detector in accordance with the High Pressure Gas Safety Law.

特開2013−22567号公報JP 2013-22567 A 特許第4652479号明細書Japanese Patent No. 4651479 特許第5095020号明細書Japanese Patent No. 5095020

本発明は上記従来技術の現状に鑑みて創案されたものであって、その目的は、簡便かつ汎用的な手法によって、液体に対して、容器のサイズを問わず、高濃度の水素を添加する手段を提供することにある。   The present invention was devised in view of the current state of the prior art, and its purpose is to add high-concentration hydrogen to a liquid regardless of the size of the container by a simple and versatile technique. It is to provide means.

上に説明したように、これまで水素水製造の分野では、水素ガスボンベや水素発生材が封入された試験管(スピッツ)を使用することしか着目されておらず、それ故に、水素水製造における簡便性および柔軟性に問題を残していた。
この問題を解消すべく本件発明者は、試行錯誤を重ねた結果、水素吸蔵合金の存在を知るに至った。水素吸蔵合金は、燃料電池の分野で多くの水素を貯蔵する手段として知られた存在であるが、これまで水素水製造の分野では着目されていなかった。
As explained above, until now, in the field of hydrogen water production, only the use of hydrogen gas cylinders and test tubes (spitz) filled with hydrogen generating materials has been focused on. Left a problem with sex and flexibility.
As a result of repeated trial and error, the present inventor has come to know the existence of a hydrogen storage alloy in order to solve this problem. Although hydrogen storage alloys are known as means for storing a lot of hydrogen in the field of fuel cells, they have not been noted in the field of hydrogen water production.

課題を解決するための手段および効果Means and effects for solving the problem

本発明は、水素吸蔵合金が保持している水素を取り出して、これを液体に添加していることが最大の特徴であり、また、それを実現するための具体的手段を種々提供するものである。
ここで言う「液体」とは、代表的には、水、お茶、コーヒー、その他のあらゆる飲料、および医療用途として使用される電解質液(生理食塩液、電解質が入った点滴液等)である。
The greatest feature of the present invention is that the hydrogen stored in the hydrogen storage alloy is taken out and added to the liquid, and various specific means for realizing it are provided. is there.
The “liquid” referred to here is typically water, tea, coffee, any other beverage, and an electrolyte solution (physiological saline solution, infusion solution containing an electrolyte, etc.) used for medical purposes.

本発明では、添加する水素を水素吸蔵合金から取り出しているので、ガスボンベを利用した大掛かりな装置に頼らずとも、家庭やオフィスにも設置可能なコンパクトな装置をもって簡便に、液体に水素を添加することが可能となる。   In the present invention, since hydrogen to be added is taken out from the hydrogen storage alloy, hydrogen can be easily added to a liquid with a compact device that can be installed in a home or office without relying on a large-scale device using a gas cylinder. It becomes possible.

本発明の水素添加方法では、液体を収容した液体容器に、水素吸蔵合金を収容した水素吸蔵合金容器を接続するとともに、水素吸蔵合金を所定温度に加温することで水素吸蔵合金容器内の水素のガス圧を高め、当該ガス圧により水素を液体容器内の液体に添加する。
この方法によれば、ガス圧を調整することで、水素が液体に添加される。すなわち、ヘンリーの法則に従い、ガス圧に応じた水素添加量が実現できるので、液体容器のサイズとは無関係に、高濃度の水素を同じように添加することが可能になる。
In the hydrogen addition method of the present invention, the hydrogen storage alloy container containing the hydrogen storage alloy is connected to the liquid container containing the liquid, and the hydrogen in the hydrogen storage alloy container is heated by heating the hydrogen storage alloy to a predetermined temperature. The gas pressure is increased, and hydrogen is added to the liquid in the liquid container by the gas pressure.
According to this method, hydrogen is added to the liquid by adjusting the gas pressure. That is, according to Henry's law, the amount of hydrogen added according to the gas pressure can be realized, so that high-concentration hydrogen can be added in the same manner regardless of the size of the liquid container.

なお、ヘンリーの法則は液体に溶け得る気体量に関する法則であって、簡単に言うと、液体に接している気体は、その圧力に比例した量で液体に溶け得る。つまり、水素ガスの圧力が高い程、多くの水素ガスが添加できることを示している。   Henry's law is a law concerning the amount of gas that can be dissolved in a liquid. In short, the gas in contact with the liquid can be dissolved in the liquid in an amount proportional to the pressure. That is, the higher the hydrogen gas pressure is, the more hydrogen gas can be added.

本発明の水素添加サーバは、「水素吸蔵合金を収容した水素吸蔵合金容器」と「当該水素吸蔵合金容器を所定温度に加温する保温器」と「流路の開閉を切り替える切替バルブ」と「外部の水素ガス供給路に接続されたとき開通し、当該接続が断たれたとき閉じる開閉手段」と「上記水素吸蔵合金容器から切替バルブに至る第1流路」と「上記切替バルブから開閉手段に至る第2流路」とを備える。
この水素添加サーバの第2流路に、液体を収容した液体容器を接続すれば、消費者は水素が添加された飲料(例えば水素水)を、飲みたい時にその場で作ることができる。あるいは、医療の場において、電解質液(生理食塩液、電解質が入った点滴液等)を必要な時に必要な量だけ作ることができる。
従来、工場で生産した水素水をペットボトルやアルミパウチや缶に封入して販売されているが、水素を添加した後、時間が経つと水素が抜けるため、水素濃度について不満があった。本発明によれば、作りたての水素水をその場で飲むことが可能となるので、このような濃度不足に関する不満が解消される。
The hydrogenation server of the present invention includes a "hydrogen storage alloy container containing a hydrogen storage alloy", a "heater that warms the hydrogen storage alloy container to a predetermined temperature", a "switching valve that switches between opening and closing of the flow path", and " Opening / closing means that opens when connected to an external hydrogen gas supply path and closes when the connection is disconnected "," first flow path from the hydrogen storage alloy container to the switching valve ", and" opening / closing means from the switching valve " 2nd flow path leading to ".
If a liquid container containing a liquid is connected to the second flow path of the hydrogenation server, the consumer can make a drink (for example, hydrogen water) to which hydrogen is added on the spot when he / she wants to drink it. Alternatively, in a medical field, an electrolyte solution (physiological saline solution, infusion solution containing an electrolyte, etc.) can be made in a necessary amount when necessary.
Conventionally, hydrogen water produced in factories has been sold in plastic bottles, aluminum pouches and cans, but since hydrogen was released over time after hydrogen was added, there was dissatisfaction with the hydrogen concentration. According to the present invention, it is possible to drink freshly prepared hydrogen water on the spot, so that such dissatisfaction with insufficient concentration is eliminated.

本発明の液体容器は、上記水素添加サーバと組み合わせて使うのに適したものである。この液体容器は、容器本体に着脱可能なキャップを備えており、キャップは、外部の水素ガス供給路に接続されたとき開通し、当該接続が断たれたとき閉じる開閉手段を備えている。
この液体容器は、水素ガス供給路を介して、上記水素添加サーバの第2流路に接続されることで、簡便な水素添加システムを構成する。
The liquid container of the present invention is suitable for use in combination with the hydrogenation server. The liquid container includes a cap that can be attached to and detached from the container main body, and the cap includes an opening / closing means that opens when connected to an external hydrogen gas supply path and closes when the connection is broken.
This liquid container constitutes a simple hydrogenation system by being connected to the second flow path of the hydrogenation server via a hydrogen gas supply path.

本発明の一実施形態に係る水素添加サーバの外観斜視図、および内部機構を併せて示す透視図。1 is an external perspective view of a hydrogenation server according to an embodiment of the present invention and a perspective view showing an internal mechanism. 図1の水素添加サーバが備える開閉手段の一例を示す斜視図。The perspective view which shows an example of the opening / closing means with which the hydrogenation server of FIG. 1 is provided. 図1の水素添加サーバ内に保持される水素吸蔵合金容器の一例を示す斜視図。The perspective view which shows an example of the hydrogen storage alloy container hold | maintained in the hydrogenation server of FIG. 図1の水素添加サーバの使用例を示す斜視図。The perspective view which shows the usage example of the hydrogenation server of FIG. 図1の水素添加サーバと使用する液体容器を例示する斜視図。The perspective view which illustrates the liquid container used with the hydrogenation server of FIG. 図5中に示した細孔フィルタの一例を示す図。The figure which shows an example of the pore filter shown in FIG.

本発明は飲料や医療用の電解質液等の液体に水素を添加することに関するが、以下の実施形態では、飲料に水素を添加する例について説明する。医療用の電解質液に対しても、同じようにして水素を添加することができる。   Although this invention relates to adding hydrogen to liquids, such as a drink and a medical electrolyte solution, the following embodiment demonstrates the example which adds hydrogen to a drink. Hydrogen can be added to the medical electrolyte solution in the same manner.

まず最初に、本発明の一実施形態に係る水素添加サーバ10について、図1を参照して説明する。この水素添加サーバ10は、スポーツクラブや家庭、オフィス、その他適当な場所に設置して、後述する液体容器内の飲料に水素を添加するのに使用される。   First, a hydrogenation server 10 according to an embodiment of the present invention will be described with reference to FIG. The hydrogen addition server 10 is installed in a sports club, home, office, or other appropriate place, and is used to add hydrogen to a beverage in a liquid container described later.

《水素添加サーバ10の構成》
図1(a)は水素添加サーバ10の外観斜視図で、図1(b)は、その主要な内部機構を併せて示す透視図である。水素添加サーバ10は、その本体内に、水素吸蔵合金容器20を、保温器30に保持した状態で収容している。さらに、水素添加サーバ10の壁面には、切替バルブ40と、流路を開閉する開閉手段51、52とが設けられている。
図1(b)に示したように、水素吸蔵合金容器20は、第1流路60を通して切替バルブ40に接続され、さらに第2流路70を通して開閉手段51、52に接続される。切替バルブ40によって、第1流路60から第2流路70に至る流路の開閉を操作することができる。第1流路60の途中には、第1圧力計65および圧力調整バルブ66が設けられている。また、第2流路70には、第2圧力計75が設けられている。
図1(b)では、第1流路60および第2流路70を模式的な直線で示しているが、実際には、これら流路はサーバ本体内で適当なチューブ材を用いて配管される。
<< Configuration of Hydrogenation Server 10 >>
FIG. 1A is an external perspective view of the hydrogenation server 10, and FIG. 1B is a perspective view showing its main internal mechanism. The hydrogenation server 10 accommodates the hydrogen storage alloy container 20 in a state in which the hydrogen storage alloy container 20 is held in the incubator 30. Furthermore, a switching valve 40 and opening / closing means 51 and 52 for opening and closing the flow path are provided on the wall surface of the hydrogenation server 10.
As shown in FIG. 1B, the hydrogen storage alloy container 20 is connected to the switching valve 40 through the first channel 60 and further connected to the opening / closing means 51 and 52 through the second channel 70. The switching valve 40 can be used to open and close the flow path from the first flow path 60 to the second flow path 70. A first pressure gauge 65 and a pressure adjustment valve 66 are provided in the middle of the first flow path 60. A second pressure gauge 75 is provided in the second flow path 70.
In FIG. 1B, the first flow path 60 and the second flow path 70 are schematically shown as straight lines. However, in actuality, these flow paths are piped using appropriate tube materials in the server body. The

《開閉手段51、52》
開閉手段51、52は、水素ガス供給チューブ(水素ガス供給路)80に接続されたとき開通し、当該接続が断たれたとき閉じるものであれば足り、その具体的構成は特定のものに限定されない。例えば、図2に示すカプラをもって開閉手段51、52とすることができる。このカプラは、ソケット55とプラグ56で構成されていて、両者が接続されたとき流路が開通し、分離されると流路が閉じる。接続されたソケット55およびプラグ56を外す際には、ソケット55の側面に設けた分離ボタン55aを押下する。
なお、ソケット55およびプラグ56のいずれか一方をもって、開閉手段51、52と把握することもできる。さらに別の例として、逆止弁を開閉手段51、52として採用してもよい。
<< Opening / closing means 51, 52 >>
The opening / closing means 51 and 52 need only be opened when connected to the hydrogen gas supply tube (hydrogen gas supply path) 80 and closed when the connection is broken, and the specific configuration is limited to a specific one. Not. For example, the opening / closing means 51 and 52 can be formed by the coupler shown in FIG. This coupler is constituted by a socket 55 and a plug 56, and when both are connected, the flow path is opened, and when separated, the flow path is closed. When the connected socket 55 and plug 56 are removed, the separation button 55 a provided on the side surface of the socket 55 is pressed.
In addition, it can also be grasped as the opening / closing means 51, 52 with either one of the socket 55 and the plug 56. As yet another example, check valves may be employed as the opening / closing means 51 and 52.

図1に示した水素添加サーバ10では、第2流路70の先端にプラグ56が設けられており、一方、外部の水素ガス供給チューブ(水素ガス供給路)80の両端にソケット55が設けられている。
In the hydrogen addition server 10 shown in FIG. 1, a plug 56 is provided at the tip of the second flow path 70, while sockets 55 are provided at both ends of an external hydrogen gas supply tube (hydrogen gas supply path) 80. ing.

《水素吸蔵合金容器20》
図1では水素吸蔵合金容器20を概略的に図示しているが、図3は、これを詳細に示している。水素吸蔵合金は、常温、低圧の条件で水素を可逆的に吸放出できる機能材料であって、常温付近で気体水素を吸収し、加熱するとその水素を放出する性質を有する。
水素吸蔵合金容器20は、水素吸蔵合金を密封状態で封入した小型の容器であって、バルブ21付きの接続管22を上部に備えている。この接続管22に、第1流路60が接続される。水素吸蔵合金容器は、例えば特開2008−180266号(出願人:日本製鋼所)に開示されたものを使用することができる。
<< Hydrogen Storage Alloy Container 20 >>
Although FIG. 1 schematically shows the hydrogen storage alloy container 20, FIG. 3 shows this in detail. The hydrogen storage alloy is a functional material capable of reversibly absorbing and releasing hydrogen under normal temperature and low pressure conditions, and has the property of absorbing gaseous hydrogen at around normal temperature and releasing the hydrogen when heated.
The hydrogen storage alloy container 20 is a small container in which a hydrogen storage alloy is sealed in a sealed state, and is provided with a connection pipe 22 with a valve 21 at the top. The first flow path 60 is connected to the connection pipe 22. As the hydrogen storage alloy container, for example, one disclosed in Japanese Patent Application Laid-Open No. 2008-180266 (Applicant: Nippon Steel Works) can be used.

水素吸蔵合金を収容してなる容器は、常用圧力が0〜0.99MPaに設定することができ、その場合には、1MPa以上にならないが故に、高圧ガス保安法でいう高圧ガスには該当しない。したがって、家庭やオフィス内で手軽に利用することが可能となる。
また、容器のサイズも直径数cm、高さ10cm程度まで小さく設計することが可能であるため、これを内蔵する水素添加サーバ10もコンパクト設計が可能となる。
さらに、水素吸蔵合金は、水素を消耗した後でも再吸収により利用可能となるため、繰返し利用によるコストダウンというメリットがある。
The container containing the hydrogen storage alloy can be set to a normal pressure of 0 to 0.99 MPa, and in that case, it does not become 1 MPa or more, and therefore does not correspond to the high pressure gas referred to in the High Pressure Gas Safety Law. . Therefore, it can be used easily in the home or office.
Moreover, since the container size can be designed to be as small as several centimeters in diameter and about 10 cm in height, the hydrogenation server 10 incorporating the container can also be compactly designed.
Furthermore, since the hydrogen storage alloy can be used by reabsorption even after depletion of hydrogen, there is an advantage of cost reduction by repeated use.

《水素添加サーバ10の使用例》
次に、図4を参照して、水素添加サーバ10の使用例を説明する。図1(a)の状態から、開閉手段51を構成するソケット55とプラグ56の接続を外して、図4(a)に示したように、当該ソケット55を液体容器100のキャップに接続する(すなわち、水素ガス供給チューブ80を液体容器100に接続する)。このとき、図4(a)において、サーバ壁面に露出したプラグ56の箇所では、第2流路70は閉止状態となっている。
詳しくは後述するが、液体容器100のキャップにも、サーバ10が備える開閉手段51、52と同様の開閉手段が設けられている。したがって、図4(a)の状態では、水素ガスは、水素ガス供給チューブ80からキャップを通過して、容器内に供給されることができる。
<< Usage example of the hydrogenation server 10 >>
Next, a usage example of the hydrogenation server 10 will be described with reference to FIG. From the state of FIG. 1A, the socket 55 constituting the opening / closing means 51 is disconnected from the plug 56, and the socket 55 is connected to the cap of the liquid container 100 as shown in FIG. That is, the hydrogen gas supply tube 80 is connected to the liquid container 100). At this time, in Fig.4 (a), the 2nd flow path 70 is a closed state in the location of the plug 56 exposed to the server wall surface.
As will be described in detail later, the cap of the liquid container 100 is also provided with opening / closing means similar to the opening / closing means 51 and 52 included in the server 10. Therefore, in the state of FIG. 4A, hydrogen gas can be supplied from the hydrogen gas supply tube 80 through the cap into the container.

保温器30を所定温度(例えば50℃)に設定して、水素吸蔵合金容器20内の水素吸蔵合金を加温すると、これにより水素吸蔵合金から水素が放出され、容器内のガス圧が上昇する。水素吸蔵合金容器20のバルブ21を開けると、放出された水素ガスは、第1流路60内に流れ込む。第1流路60内のガス圧は、第1圧力計65で読むことができる。
第1流路60に設けた圧力調整バルブ66を操作して、第1流路60内のガス圧を調整する。
When the incubator 30 is set to a predetermined temperature (for example, 50 ° C.) and the hydrogen storage alloy in the hydrogen storage alloy container 20 is heated, hydrogen is released from the hydrogen storage alloy and the gas pressure in the container increases. . When the valve 21 of the hydrogen storage alloy container 20 is opened, the released hydrogen gas flows into the first flow path 60. The gas pressure in the first flow path 60 can be read by the first pressure gauge 65.
The gas pressure in the first flow path 60 is adjusted by operating the pressure adjustment valve 66 provided in the first flow path 60.

第1流路60内のガス圧が所定値(例えば0.5MPa)に達したら、切替バルブ40を操作して、第1流路60から第2流路70に至る流路を開通させる。これにより、水素ガスは、第2流路70から水素ガス供給チューブ80を通して、液体容器100内に供給され、ヘンリーの法則に従い容器内の飲料に添加される。この時の水素ガス圧は、第2圧力計75で読むことができ、例えば0.2〜0.5MPa程度に設定する。   When the gas pressure in the first flow path 60 reaches a predetermined value (for example, 0.5 MPa), the switching valve 40 is operated to open the flow path from the first flow path 60 to the second flow path 70. Thus, the hydrogen gas is supplied from the second flow path 70 through the hydrogen gas supply tube 80 into the liquid container 100 and added to the beverage in the container according to Henry's law. The hydrogen gas pressure at this time can be read by the second pressure gauge 75, and is set to about 0.2 to 0.5 MPa, for example.

常温・常圧では、ヘンリーの法則に従い1.6ppm以下の水素濃度しか実現できないこととなるが、本発明では、水素吸蔵合金を加温して得られるガス圧を利用して水素を添加するので、供給時のガス圧を制御することで、高濃度(5ppm)または超高濃度(6ppm)で水素を添加することが可能となる。   At room temperature and normal pressure, only hydrogen concentration of 1.6 ppm or less can be realized according to Henry's law. However, in the present invention, hydrogen is added using the gas pressure obtained by heating the hydrogen storage alloy. By controlling the gas pressure at the time of supply, hydrogen can be added at a high concentration (5 ppm) or an ultrahigh concentration (6 ppm).

また、ガス圧に応じて水素添加量をコントロールできるので、液体容器のサイズとは無関係に、所望の濃度で水素を添加することが可能になる。1回で飲み切れるサイズ(例えば、150〜200ml)の液体容器を用いれば、水素を添加したての飲料をその場で全て飲み切ってしまうことができる。従来、工場で生産した水素水をペットボトルやアルミパウチや缶に封入して販売されているが、水素を添加した後、時間が経つと水素が抜けるため、水素濃度について不満があった。本発明によれば、そのような不満は完全に解消できる。   In addition, since the amount of hydrogen added can be controlled according to the gas pressure, it is possible to add hydrogen at a desired concentration regardless of the size of the liquid container. If a liquid container having a size that can be swallowed at once (for example, 150 to 200 ml) is used, it is possible to swallow all the freshly added beverage on the spot. Conventionally, hydrogen water produced in factories has been sold in plastic bottles, aluminum pouches and cans, but since hydrogen was released over time after hydrogen was added, there was dissatisfaction with the hydrogen concentration. According to the present invention, such dissatisfaction can be completely eliminated.

図4(b)は、別の使用態様を示している。すなわち、水素添加サーバ10に2系統以上の水素ガス供給チューブ80a、80bを接続すれば、2以上の液体容器100に並行して同時に水素ガスを供給することができる。図4(b)では、一方のチューブ80bとして途中で2つに分岐するものを使用し、合計3つの液体容器100に同時に水素ガスを供給している。両方のチューブを共に分岐させることや、共に分岐しないものを使用することも可能である。
さらに、図示はしていないが第2流路70を3系統以上に分岐させる(それに合わせ、開閉手段を3つ以上設ける)ことも可能である。
このような複数系統を利用する場合、例えば、異なるサイズの容器に同時に水素ガスを供給することや、異なる液体に同時に水素ガスを供給することが可能となる。
FIG. 4B shows another usage mode. That is, if two or more systems of hydrogen gas supply tubes 80 a and 80 b are connected to the hydrogenation server 10, hydrogen gas can be supplied simultaneously to two or more liquid containers 100. In FIG. 4B, one tube 80 b that branches into two in the middle is used, and hydrogen gas is simultaneously supplied to a total of three liquid containers 100. It is also possible to branch both tubes together, or to use one that does not branch together.
Further, although not shown, the second flow path 70 can be branched into three or more systems (three or more opening / closing means are provided accordingly).
When such a plurality of systems are used, for example, it is possible to supply hydrogen gas simultaneously to containers of different sizes, or to supply hydrogen gas simultaneously to different liquids.

《液体容器100》
図4では液体容器100を概略的に示しているが、これを、図5を参照して詳しく説明する。液体容器100は、水素添加対象となる液体を収容しており、そのキャップ101に開閉手段を備えている。開閉手段は、水素ガス供給チューブ80に接続されたとき開通し、当該接続が断たれたとき閉じるものであれば足り、その具体的構成は特定のものに限定されない。
図5の例では、図2に示したカプラ中のプラグ56が開閉手段を構成している。なお、ソケット55、あるいはソケット55とプラグ56で構成されるカプラ全体をキャップに備えて、これを開閉手段とすることもできる。
いずれの場合でも、液体容器100は、水素ガス供給チューブ80に接続される前は、キャップ101によって密封された状態となり、水素ガス供給チューブ80に接続されると、水素ガス供給チューブ80からの水素ガスが容器内に進入することが可能となる。
<< Liquid container 100 >>
FIG. 4 schematically shows the liquid container 100, which will be described in detail with reference to FIG. The liquid container 100 contains a liquid to be hydrogenated, and the cap 101 is provided with an opening / closing means. The opening / closing means need only be opened when connected to the hydrogen gas supply tube 80 and closed when the connection is broken, and its specific configuration is not limited to a specific one.
In the example of FIG. 5, the plug 56 in the coupler shown in FIG. 2 constitutes an opening / closing means. Note that the socket 55 or the entire coupler including the socket 55 and the plug 56 may be provided in the cap, and this may be used as the opening / closing means.
In any case, the liquid container 100 is sealed by the cap 101 before being connected to the hydrogen gas supply tube 80, and when connected to the hydrogen gas supply tube 80, the hydrogen from the hydrogen gas supply tube 80 is Gas can enter the container.

図5(a)では、プラグ56からチューブ105を飲料内にまで延在させており、したがって、水素ガスが飲料内部に直接供給させることとなるので、水素添加効率が高まると考えられる。ただし、ヘンリーの法則に従いガス圧に応じた水素添加量が得られるので、チューブ105を省略することも可能である。   In FIG. 5A, the tube 105 is extended from the plug 56 to the inside of the beverage. Therefore, hydrogen gas is directly supplied into the inside of the beverage, so that it is considered that the hydrogenation efficiency is increased. However, the amount of hydrogen added according to the gas pressure can be obtained in accordance with Henry's law, so that the tube 105 can be omitted.

さらに別例として、図5(b)に示したように、キャップに設けた開閉手段(プラグ56)よりも下流側に細孔フィルタ200を設けてもよい。細孔フィルタ200は細孔濾過膜を内部に備えていて、供給される水素ガスは、この細孔を通過しマイクロバブルとなって飲料内に噴出する。
なお、図示はしていないが、細孔フィルタ200は、水素添加サーバ10内の第1流路60あるいは第2流路70に設けてもよい。
As another example, as shown in FIG. 5B, a pore filter 200 may be provided on the downstream side of the opening / closing means (plug 56) provided in the cap. The pore filter 200 includes a pore filtration membrane inside, and the supplied hydrogen gas passes through the pores and becomes microbubbles, which are ejected into the beverage.
Although not shown, the pore filter 200 may be provided in the first flow path 60 or the second flow path 70 in the hydrogenation server 10.

細孔濾過膜の孔径は特に限定されるものではないが、例えば孔径30μm以下、あるいは10μmとすることが考えられる。孔径が小さくなる程、フィルタは高価になるので、コスト面を考えて、例えば、次のように設定することができる。
(ア)各液体容器内にそれぞれ細孔フィルタ200を設ける場合には、比較的安価な孔径30μm以下のものを採用して、コスト増を抑える。
(イ)水素添加サーバ10内の第1流路60あるいは第2流路70に細孔フィルタ200を設ける場合には、これをもって全ての液体容器に対応できるので、比較的高価ではあるが孔径10μm以下のものを採用する。
The pore diameter of the pore filtration membrane is not particularly limited, but for example, the pore diameter may be 30 μm or less or 10 μm. The smaller the hole diameter, the more expensive the filter. For example, the following setting can be made in consideration of cost.
(A) When the pore filter 200 is provided in each liquid container, a relatively inexpensive one having a pore diameter of 30 μm or less is employed to suppress an increase in cost.
(A) When the pore filter 200 is provided in the first flow path 60 or the second flow path 70 in the hydrogenation server 10, since it can be used for all liquid containers, it is relatively expensive but has a pore diameter of 10 μm. Use the following:

細孔フィルタ200として、公知のものを適宜採用することが可能であるが、例えば、「株式会社日本ピスコ製のST6(サイレンサ)」や「株式会社伏見製薬所製のテクノポーラス(登録商標)IWX」を利用することが可能である。
「ST6(サイレンサ)」は、本来、機器の排気ポートに取り付けて排気音を軽減するサイレンサとして開発されたものであるが、孔径10μm程度の細孔を有しており、本願発明において細孔フィルタ200として使用することが可能である。一方、「テクノポーラス(登録商標)IWX」は、本来、吸水性に優れたスポンジとして開発されたものであるが、孔径1μm程度の細孔を有しており、本願発明において細孔フィルタ200として使用することが可能である。
As the pore filter 200, a known filter can be appropriately used. For example, "ST6 (silencer) manufactured by Nippon Pisco Co., Ltd." or "Technoporous (registered trademark) IWX manufactured by Fushimi Pharmaceutical Co., Ltd." Can be used.
"ST6 (silencer)" was originally developed as a silencer that is attached to the exhaust port of equipment to reduce exhaust noise, and has pores with a pore diameter of about 10 µm. 200 can be used. On the other hand, “Technoporous (registered trademark) IWX” was originally developed as a sponge having excellent water absorption, but has pores with a pore diameter of about 1 μm. It is possible to use.

《細孔フィルタ200を設けてマイクロバブルを作ることのメリット》
マイクロバブルによるメリットとしては、次のようなものがある。
(1)
通常の気泡は急激に水液中を上昇し最終的に液面で破裂するが、マイクロバブルは、気泡体積が微細であるが故に上昇速度が遅いので、長時間水液中に滞在し続ける。つまり、水素ガスの添加量の増大が期待できる。例えば、直径10μmの気泡は一分間に3mm程度しか上昇しない。
(2)
気相と液相の間には界面張力が生じるが、気泡の大きさに反比例して気泡に加わる圧力が高まる。このため、マイクロバブルは圧力で一層小さくなり、さらに圧力が高まる。理論上、無限の圧力が生じる。そして、ヘンリーの法則に従い、水素ガスの添加量の増大が期待できる。
(3)
細孔を通過して形成されたマイクロバブルは、一般に負に帯電していて、マイクロバブル同士が反発し合う。この性質のため、マイクロバブル同士が結合して大きくなることは起こらず、したがって、上記(1)、(2)の効果が減じられることがない。
<< Advantages of Producing Micro Bubbles with Pore Filter 200 >>
Advantages of microbubbles include the following.
(1)
Ordinary bubbles rapidly rise in the liquid and finally rupture at the liquid level, but microbubbles keep staying in the liquid for a long time because the bubble volume is fine and the rising speed is slow. That is, an increase in the amount of hydrogen gas added can be expected. For example, a 10 μm diameter bubble rises only about 3 mm per minute.
(2)
Interfacial tension is generated between the gas phase and the liquid phase, but the pressure applied to the bubbles increases in inverse proportion to the size of the bubbles. For this reason, the microbubbles become smaller with pressure, and the pressure further increases. Theoretically, infinite pressure occurs. An increase in the amount of hydrogen gas added can be expected according to Henry's law.
(3)
The microbubbles formed through the pores are generally negatively charged and the microbubbles repel each other. Due to this property, the microbubbles do not increase in size due to bonding, and therefore the effects (1) and (2) are not reduced.

《細孔フィルタ200の具体例》
細孔フィルタ200の具体的構成は特定のものに限定されないが、その一例を図6に示した。図6の例では、細孔フィルタ200は、多数の中空糸201からなる中空糸膜を収容している。
各中空糸201は、U字状に折り返されていて、両端がポッティング部202で固定されて水素ガスの供給側に開口している。水素添加サーバ10から供給される水素ガスは、この開口から中空糸201に入り、中空糸壁面の細孔を通過して飲料内に放出される。
<< Specific Example of Pore Filter 200 >>
The specific configuration of the pore filter 200 is not limited to a specific one, but an example thereof is shown in FIG. In the example of FIG. 6, the pore filter 200 accommodates a hollow fiber membrane composed of a large number of hollow fibers 201.
Each hollow fiber 201 is folded in a U shape, and both ends are fixed by a potting portion 202 and open to the hydrogen gas supply side. Hydrogen gas supplied from the hydrogenation server 10 enters the hollow fiber 201 through this opening, passes through the pores of the hollow fiber wall surface, and is released into the beverage.

水素ガスが細孔を高速通過することにより静電気を起こし、負に帯電したマイクロバブルとなる。特に図6に示した構成によれば、水素ガスがポッティング部202を通過して中空糸201内に入る際、オリフィス効果により水素ガスの速度が増し、その分だけマイクロバブルが勢いよく飲料内に飛び込むため、水素添加効率の向上が期待できる。
When the hydrogen gas passes through the pores at high speed, static electricity is generated, resulting in negatively charged microbubbles. In particular, according to the configuration shown in FIG. 6, when hydrogen gas passes through the potting portion 202 and enters the hollow fiber 201, the velocity of the hydrogen gas increases due to the orifice effect, and the microbubbles vigorously enter the beverage. Because it jumps in, it can be expected to improve hydrogenation efficiency.

《実施例1》
図6に示したような細孔フィルタ200(ポリオレフィン製、孔径0.01μm)を用いた場合の効果を確かめるべく実験を行った。200mlの容器に水道水を入れ、注入圧力0.23MPaで水素ガスを添加した後、30秒撹拌し、酸化還元電位(ORP)を測定した。なお、水素ガス添加前の酸化還元電位は206mVであった。
水素ガス添加後の酸化還元電位は、細孔フィルタ無しの場合が−70mVで、細孔フィルタ有りの場合が−128mVであった。
Example 1
An experiment was conducted to confirm the effect of using the pore filter 200 (made of polyolefin, pore size 0.01 μm) as shown in FIG. Tap water was put into a 200 ml container, hydrogen gas was added at an injection pressure of 0.23 MPa, and the mixture was stirred for 30 seconds, and the oxidation-reduction potential (ORP) was measured. The oxidation-reduction potential before addition of hydrogen gas was 206 mV.
The oxidation-reduction potential after addition of hydrogen gas was −70 mV without the pore filter and −128 mV with the pore filter.

なお、酸化還元電位(Oxidation Reduction Potential)とは、一般的に知られた指標であって、ある物質が他の物質を酸化しやすい状態にあるのか、または還元しやすい状態にあるのかを示すものである。この値がプラスで大きければ酸化力が強く、マイナスで大きければ還元力が強いことを意味している。   Oxidation Reduction Potential is a generally known index that indicates whether a substance is easily oxidized or easily reduced by another substance. It is. If this value is positive and large, the oxidizing power is strong, and if it is negative and large, it means that the reducing power is strong.

上記実験の結果、細孔フィルタ200無しでも酸化還元電位の低下が認められるが、細孔フィルタ200を使用することで、酸化還元電位の低下がより顕著であること(すなわち、水素ガス添加の効果が高いこと)が確認できた。   As a result of the above experiment, a reduction in oxidation-reduction potential is observed without the pore filter 200, but the reduction in oxidation-reduction potential is more remarkable by using the pore filter 200 (that is, the effect of hydrogen gas addition). Was high).

《実施例2》
また、電解質液に対しても水素ガスの添加が可能であることを確認するために、細孔フィルタ200を使用し、株式会社大塚製薬工場が提供する経口補水液(OS−1、登録商標)に対して、上記実施例1と同じ実験を行った。
その結果、水素ガス添加前の酸化還元電位212mVが、水素添加後には−83mVと低下しており、このような電解質液に対しても水素ガスの添加が可能であることが確認できた。
Example 2
In addition, in order to confirm that hydrogen gas can be added to the electrolyte solution, an oral rehydration solution (OS-1, registered trademark) provided by Otsuka Pharmaceutical Factory Co., Ltd. using a pore filter 200 is used. In contrast, the same experiment as in Example 1 was performed.
As a result, the oxidation-reduction potential 212 mV before the addition of hydrogen gas decreased to −83 mV after the addition of hydrogen, and it was confirmed that hydrogen gas could be added to such an electrolyte solution.

《その他》
水素吸蔵合金から取り出した水素が添加されてなる液体は、図1に示したようなサーバ類を省略して、液体容器100と水素吸蔵合金容器20と直接(あるいは、単なるチューブ材のみを介して)接続して、製造することも考えられる。最も簡単な想定として、片手で持てる小サイズの水素吸蔵合金容器20と液体容器100をバッグ等に入れて持ち運ぶようにすれば、街角や公園のベンチ等、場所を問わずに、飲料に水素を添加してその場で飲用することが可能となる。
ただし、その場合には、外気温あるいは体温を利用して水素吸蔵合金を加温することとなり、それ故、水素ガスの添加圧力、ひいては水素濃度にバラツキが出る。水素濃度にバラツキがあっても水素水飲用による効果が得られるが、このバラツキを無くすためには、保温器を備えた水素添加サーバを利用するのが好ましい。
<Others>
The liquid to which hydrogen extracted from the hydrogen storage alloy is added omits the servers as shown in FIG. 1, and is directly connected to the liquid container 100 and the hydrogen storage alloy container 20 (or only through a simple tube material). ) It is also possible to connect and manufacture. The simplest assumption is that if you hold a small-sized hydrogen storage alloy container 20 and liquid container 100 that can be held with one hand in a bag, you can carry hydrogen in your beverage regardless of the location, such as street corners or park benches. It can be added and consumed on the spot.
However, in that case, the hydrogen storage alloy is heated using the outside air temperature or body temperature, and therefore, the addition pressure of hydrogen gas and thus the hydrogen concentration varies. Even if there is a variation in the hydrogen concentration, the effect of drinking hydrogen water can be obtained. However, in order to eliminate this variation, it is preferable to use a hydrogenation server equipped with a warmer.

10 水素添加サーバ
20 水素吸蔵合金容器
21 バルブ
22 接続管
30 保温器
40 切替バルブ
51、52 開閉手段
55 ソケット
56 プラグ
60 第1流路
65 第1圧力計
66 圧力調整バルブ
70 第2流路
75 第2圧力計
80 水素ガス供給チューブ
100 飲料容器(液体容器)
101 キャップ
200 細孔フィルタ
201 中空糸
202 ポッティング部
DESCRIPTION OF SYMBOLS 10 Hydrogenation server 20 Hydrogen storage alloy container 21 Valve 22 Connection pipe 30 Insulator 40 Switching valve 51, 52 Opening and closing means 55 Socket 56 Plug 60 First flow path 65 First pressure gauge 66 Pressure adjustment valve 70 Second flow path 75 First 2 Pressure gauge 80 Hydrogen gas supply tube 100 Beverage container (liquid container)
101 Cap 200 Pore filter 201 Hollow fiber 202 Potting part

Claims (7)

下記水素添加サーバ(10)の開閉手段と、下記液体容器(100)の開閉手段と、を互いに着脱可能に接続して構成される水素添加システムであって、
水素添加サーバ(10)の圧力調整バルブ(66)でガス圧を調整し、液体容器(100)内の圧力を高めて、所望濃度で液体容器(100)内の液体に水素を添加する、水素添加システム。

《水素添加サーバ》
水素吸蔵合金を収容した水素吸蔵合金容器(20)と、
当該水素吸蔵合金容器を所定温度に加温する保温器(30)と、
流路の開閉を切り替える切替バルブ(40)と、
外部の水素ガス供給路に接続されたとき開通し、当該接続が断たれたとき閉じる開閉手段(51、52、55、56)と、
上記水素吸蔵合金容器から切替バルブに至る第1流路(60)と、
上記切替バルブから開閉手段に至る第2流路(70)と、
上記第1流路(60)に設けた圧力調整バルブ(66)とを備える、水素添加サーバ(10)。

《液体容器》
容器本体に着脱可能なキャップ(101)を備えた液体容器であって、
キャップ(101)は、外部の水素ガス供給路に接続されたとき開通し、当該接続が断たれたとき閉じる開閉手段(55、56)を備えている、液体容器(100)。
A hydrogenation system configured by detachably connecting an opening / closing means of the following hydrogenation server (10) and an opening / closing means of the following liquid container (100),
Hydrogen that adjusts the gas pressure with the pressure regulating valve (66) of the hydrogenation server (10), increases the pressure in the liquid container (100), and adds hydrogen to the liquid in the liquid container (100) at a desired concentration. Additive system.

《Hydrogenation server》
A hydrogen storage alloy container (20) containing a hydrogen storage alloy;
A warmer (30) for heating the hydrogen storage alloy container to a predetermined temperature;
A switching valve (40) for switching opening and closing of the flow path;
Opening / closing means (51, 52, 55, 56) that opens when connected to an external hydrogen gas supply path and closes when the connection is disconnected;
A first flow path (60) from the hydrogen storage alloy container to the switching valve;
A second flow path (70) from the switching valve to the opening / closing means;
The hydrogenation server (10) provided with the pressure regulation valve (66) provided in the said 1st flow path (60).

《Liquid container》
A liquid container having a cap (101) detachably attached to the container body,
The cap (101) is provided with opening / closing means (55, 56) that is opened when connected to an external hydrogen gas supply path and closed when the connection is broken.
下記水素添加サーバ(10)の開閉手段と、下記液体容器(100)の開閉手段と、を互いに着脱可能に接続して構成される水素添加システムであって、
水素添加サーバ(10)の圧力調整バルブ(66)でガス圧を調整し、液体容器(100)内の圧力を高めて、所望濃度で液体容器(100)内の液体に水素を添加する、水素添加システム。

《水素添加サーバ》
水素吸蔵合金を収容した水素吸蔵合金容器(20)と、
外部の水素ガス供給路に接続されたとき開通し、当該接続が断たれたとき閉じる開閉手段(51、52、55、56)と、
上記水素吸蔵合金容器から開閉手段に至る流路(60、70)と、
上記流路に設けた圧力調整バルブ(66)とを備える、水素添加サーバ(10)。

《液体容器》
容器本体に着脱可能なキャップ(101)を備えた液体容器であって、
キャップ(101)は、外部の水素ガス供給路に接続されたとき開通し、当該接続が断たれたとき閉じる開閉手段(55、56)を備えている、液体容器(100)。
A hydrogenation system configured by detachably connecting an opening / closing means of the following hydrogenation server (10) and an opening / closing means of the following liquid container (100),
Hydrogen that adjusts the gas pressure with the pressure regulating valve (66) of the hydrogenation server (10), increases the pressure in the liquid container (100), and adds hydrogen to the liquid in the liquid container (100) at a desired concentration. Additive system.

《Hydrogenation server》
A hydrogen storage alloy container (20) containing a hydrogen storage alloy;
Opening / closing means (51, 52, 55, 56) that opens when connected to an external hydrogen gas supply path and closes when the connection is disconnected;
A flow path (60, 70) from the hydrogen storage alloy container to the opening / closing means;
A hydrogenation server (10) comprising a pressure regulating valve (66) provided in the flow path.

《Liquid container》
A liquid container having a cap (101) detachably attached to the container body,
The cap (101) is provided with opening / closing means (55, 56) that is opened when connected to an external hydrogen gas supply path and closed when the connection is broken.
上記水素添加サーバ(10)の開閉手段と、液体容器(100)の開閉手段とが、水素ガス供給路(80)によって接続されている、請求項1または2記載の水素添加システム。
The hydrogenation system according to claim 1 or 2, wherein the opening / closing means of the hydrogenation server (10) and the opening / closing means of the liquid container (100) are connected by a hydrogen gas supply path (80).
上記水素添加サーバが、開閉手段(51、52、55、56)を複数備えるとともに、上記第2流路(70)または流路が途中で複数に分岐して各開閉手段に至る、請求項1〜3のいずれか1つに記載の水素添加システム。
The hydrogenation server includes a plurality of opening / closing means (51, 52, 55, 56), and the second flow path (70) or the flow path is branched into a plurality in the middle to reach each opening / closing means. The hydrogenation system as described in any one of -3.
上記水素添加サーバ(10)の開閉手段と、上記液体容器(100)の開閉手段は、それぞれ、着脱可能なプラグ(56)およびソケット(55)の一方または両方で構成されている、請求項1〜3のいずれか1つに記載の水素添加システム。
The opening / closing means of the hydrogenation server (10) and the opening / closing means of the liquid container (100) are each constituted by one or both of a detachable plug (56) and a socket (55). The hydrogenation system as described in any one of -3.
請求項1〜3のいずれか1つに記載の水素添加システムに使用する液体容器(100)であって、
容器本体に着脱可能なキャップ(101)を備えていて、
キャップ(101)は、外部の水素ガス供給路に接続されたとき開通し、当該接続が断たれたとき閉じる開閉手段(55、56)を備えている、液体容器。
A liquid container (100) for use in a hydrogenation system according to any one of claims 1-3,
The container body is equipped with a removable cap (101),
The cap (101) is a liquid container provided with opening / closing means (55, 56) that opens when connected to an external hydrogen gas supply path and closes when the connection is broken.
上記開閉手段は、着脱可能なプラグ(56)およびソケット(55)の一方または両方で構成されている、請求項6記載の液体容器。   The liquid container according to claim 6, wherein the opening / closing means comprises one or both of a detachable plug (56) and a socket (55).
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