JP6051267B1 - Electrolysis tank for electrolytic hydrogen gas generator - Google Patents

Electrolysis tank for electrolytic hydrogen gas generator Download PDF

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JP6051267B1
JP6051267B1 JP2015108776A JP2015108776A JP6051267B1 JP 6051267 B1 JP6051267 B1 JP 6051267B1 JP 2015108776 A JP2015108776 A JP 2015108776A JP 2015108776 A JP2015108776 A JP 2015108776A JP 6051267 B1 JP6051267 B1 JP 6051267B1
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hydrogen gas
gas generation
generation tank
ion exchange
tank
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JP2016222961A (en
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中村 寅雄
寅雄 中村
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TR & K CORP.
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Abstract

【課題】イオン交換膜を用いて水の電気分解を行う水素ガス発生装置の電気分解槽において、イオン交換膜と電極とを簡易な手段で固定し、イオン交換膜の破損を防ぐ。【解決手段】水の電気分解を行う電気分解槽1は、イオン交換膜IEにより水素ガス発生槽1Hと酸素ガス発生槽1Oとに分割されている。イオン交換膜IEの両側には、直流電源の陽極及び陰極に接続される電極板2P、2Mがそれぞれ設置され、これらは、水素ガス発生槽1Hのケース1HCと酸素ガス発生槽1Oのケース1OCとを通しボルト等で締め付けることにより、互いに密着した状態で固定される。水を貯留する水素ガス発生槽1Hと酸素ガス発生槽1Oの空間部には、その周縁部及び中央部に、電極板2P、2Mをイオン交換膜IEに押し付けるリブが設けてある。【選択図】図2In an electrolysis tank of a hydrogen gas generator that performs electrolysis of water using an ion exchange membrane, the ion exchange membrane and an electrode are fixed by simple means to prevent the ion exchange membrane from being damaged. An electrolysis tank 1 for electrolyzing water is divided into a hydrogen gas generation tank 1H and an oxygen gas generation tank 1O by an ion exchange membrane IE. On both sides of the ion exchange membrane IE, electrode plates 2P and 2M connected to the anode and the cathode of the DC power source are respectively installed. These are the case 1HC of the hydrogen gas generation tank 1H and the case 1OC of the oxygen gas generation tank 1O. By tightening with a bolt or the like, they are fixed in close contact with each other. In the space between the hydrogen gas generation tank 1H and the oxygen gas generation tank 1O for storing water, ribs for pressing the electrode plates 2P and 2M against the ion exchange membrane IE are provided at the peripheral edge and the center. [Selection] Figure 2

Description

本発明は、イオン交換膜を用いて水を電気分解し水素ガスを発生する装置、特に、循環ポンプ等の大掛かりな設備が不要で、一般家庭などに設置して簡易に使用することができる小型の電解式水素ガス発生装置に関するものである。   The present invention eliminates the need for large equipment such as a circulation pump, which is an apparatus that electrolyzes water using an ion exchange membrane to generate hydrogen gas, and can be easily installed and used in a general household. The present invention relates to an electrolytic hydrogen gas generator.

水の電気分解により水素ガスを発生させ、この水素ガスを食品や飲料品に溶解させたり体内に直接吸入したりすることで、過酸化物の還元を行う、あるいは食品等の酸化による劣化を防止する方法が、従来から知られている。一例として、特開2004−350538号公報には、水で満たした電気分解槽の内部をイオン交換膜(固体高分子膜)により2つに分割し、イオン交換膜の両面に直流電圧を印加して陰極側から水素ガスを発生させ、その水素ガスをコップ内の液体飲料に溶解する装置が開示されている。   Hydrogen is generated by electrolysis of water, and this hydrogen gas is dissolved in foods and beverages or directly inhaled into the body to reduce peroxides or prevent deterioration of foods due to oxidation The method of doing is known conventionally. As an example, Japanese Patent Application Laid-Open No. 2004-350538 discloses that an electrolysis tank filled with water is divided into two by an ion exchange membrane (solid polymer membrane), and a DC voltage is applied to both surfaces of the ion exchange membrane. An apparatus for generating hydrogen gas from the cathode side and dissolving the hydrogen gas in a liquid beverage in a cup is disclosed.

また、特開2014−19950号公報には、イオン交換膜とその両面にそれぞれ密着する一対の電極板により電気分解板を構成し、電気分解板を仕切板として両側に水素ガス発生槽及び酸素ガス発生槽を設けた卓上型水素ガス発生装置が開示されている。この卓上型水素ガス発生装置は、純水を電気分解して、発生した水素ガスを体内への吸引、科学実験等に利用する装置であって、図5にその概要を示す。
図5において、電気分解槽1にはイオン交換膜を一対の電極板で挟んだ電気分解板20が設置され、電気分解槽1は、陰極側の水素ガス発生槽1Hと陽極側の酸素ガス発生槽1Oとに分割される。A部拡大図に示すとおり、電気分解板20は、イオン交換膜IEの両面に孔の開いた網目状の電極板2P、2Mを密着させたもので、イオン交換膜及び2枚の電極板は、樹脂製のリベット21でかしめることにより一体的に結合される。また、イオン交換膜IEは電極板よりも外側に広がっており、B部拡大図に示すとおり、その外側の部分を水素ガス発生槽1Hのケースと酸素ガス発生槽1Oのケースとで挟み込むことにより、電気分解板20は、電気分解槽1に固定される。水素ガス発生槽1H側の電極板2Mは直流電源の−側に、酸素ガス発生槽1O側の電極板2Pは直流電源の+側にそれぞれ接続される。
Japanese Patent Laid-Open No. 2014-19950 discloses an electrolysis plate composed of an ion exchange membrane and a pair of electrode plates that are in close contact with both sides thereof, and a hydrogen gas generation tank and oxygen gas are formed on both sides using the electrolysis plate as a partition plate. A desktop hydrogen gas generator provided with a generation tank is disclosed. This desktop hydrogen gas generator is an apparatus that electrolyzes pure water and uses the generated hydrogen gas for suction into the body, scientific experiments, etc., and its outline is shown in FIG.
In FIG. 5, an electrolysis plate 20 having an ion exchange membrane sandwiched between a pair of electrode plates is installed in the electrolysis bath 1, and the electrolysis bath 1 generates a hydrogen gas generation bath 1H on the cathode side and an oxygen gas generation on the anode side. Divided into a tank 1O. As shown in the enlarged view of the part A, the electrolysis plate 20 is a plate in which mesh-like electrode plates 2P and 2M having holes are adhered to both surfaces of the ion exchange membrane IE. The ion exchange membrane and the two electrode plates are These are integrally joined by caulking with a resin rivet 21. In addition, the ion exchange membrane IE spreads outside the electrode plate, and as shown in the enlarged view of part B, the outer part is sandwiched between the case of the hydrogen gas generation tank 1H and the case of the oxygen gas generation tank 1O. The electrolysis plate 20 is fixed to the electrolysis tank 1. The electrode plate 2M on the hydrogen gas generation tank 1H side is connected to the negative side of the DC power source, and the electrode plate 2P on the oxygen gas generation tank 1O side is connected to the positive side of the DC power source.

電気分解によって水素ガス発生槽1Hに生成された水素ガスは、水素ガス取出し管PHを経由して洗浄ビン3に導かれる。洗浄ビン3には所定の水位となるように浄水が入れられており、水素ガス取出し管HPは、洗浄ビン3の底部付近に開口するので、水素ガス発生槽1Hの水素ガスには水圧によって一定の圧力が作用している。洗浄ビン3の上部に溜まった水素ガスは、抽出管4から体内への吸入等使用目的に応じて送出される。また、電気分解槽1に純水を供給するための給水タンク5が設置されており、給水タンク5の底部は、連通管により水素ガス発生槽1H及び酸素ガス発生槽1Oの底部とそれぞれ連結されている。   The hydrogen gas generated in the hydrogen gas generation tank 1H by the electrolysis is guided to the cleaning bottle 3 via the hydrogen gas take-out pipe PH. The cleaning bottle 3 is filled with purified water so as to have a predetermined water level, and the hydrogen gas extraction pipe HP opens near the bottom of the cleaning bottle 3, so that the hydrogen gas in the hydrogen gas generation tank 1H is constant depending on the water pressure. Pressure is acting. The hydrogen gas accumulated in the upper part of the washing bottle 3 is sent out from the extraction tube 4 according to the purpose of use such as inhalation into the body. Further, a water supply tank 5 for supplying pure water to the electrolysis tank 1 is installed, and the bottom of the water supply tank 5 is connected to the bottom of the hydrogen gas generation tank 1H and the oxygen gas generation tank 1O by a communication pipe. ing.

ところで、電気分解板20に直流電圧を印加し電気分解を行う過程では、電気泳動によって酸素ガス発生槽1Oの純水が水素ガス発生槽1Hに移動したり、電気分解板20で発生する熱により電気分解槽1内の純水が蒸発したりして、両方のガス発生槽に水位差が生じる。そして、水素ガス発生槽1Hに加わる圧力(洗浄ビン3の水中への放出に伴う背圧)は、底部の連通管を介して酸素ガス発生槽1Oにも作用し、水位差が大きくなると酸素ガス発生槽1Oから純水が溢れたり、電気分解板20に働く水圧の差に起因して、ケースに挟まれたイオン交換膜IEが破損する恐れがある。
水素ガス発生槽1Hの圧力に対抗するため、酸素ガス発生槽1Oの上部には、ステンレス等の鋼球BLを用いた保圧弁(逆止弁)が弁座VSに接するようにして設置されており、酸素ガス発生槽1Oの圧力が所定の値となって鋼球BLを押し上げるまで、酸素ガスの放出を防止している。これにより、両方のガス発生槽の水位をバランスさせて、過剰の水位差の発生を防いでいる。
By the way, in the process of applying a DC voltage to the electrolysis plate 20 to perform electrolysis, the pure water in the oxygen gas generation tank 1O moves to the hydrogen gas generation tank 1H by electrophoresis, or by heat generated in the electrolysis plate 20. The pure water in the electrolysis tank 1 evaporates, causing a difference in water level between both gas generation tanks. The pressure applied to the hydrogen gas generation tank 1H (back pressure associated with the discharge of the cleaning bottle 3 into the water) also acts on the oxygen gas generation tank 1O through the bottom communication pipe, and the oxygen gas increases when the water level difference increases. There is a possibility that the pure water overflows from the generation tank 1O or the ion exchange membrane IE sandwiched between the cases is damaged due to a difference in water pressure acting on the electrolysis plate 20.
In order to counter the pressure of the hydrogen gas generation tank 1H, a pressure holding valve (check valve) using a steel ball BL such as stainless steel is installed on the upper part of the oxygen gas generation tank 1O in contact with the valve seat VS. The release of oxygen gas is prevented until the pressure in the oxygen gas generation tank 1O reaches a predetermined value and pushes up the steel ball BL. Thereby, the water level of both gas generation tanks is balanced, and generation | occurrence | production of an excessive water level difference is prevented.

特開2004−350538号公報JP 2004-350538 A 特開2014−19950号公報JP 2014-19950 A

図5の水素ガス発生装置は、イオン交換膜を用いて純水を電気分解するものであり、純水を使用するため不純物の析出等に起因する装置の劣化が生じることはなく、耐用年数の長い装置である。また、循環ポンプ等の大掛かりな設備が不要な小型の装置であって、一般家庭などの使用に好適であるが、イオン交換膜と電極板とを組み合わせた電気分解板の構造、あるいは、水素ガス発生槽1Hと酸素ガス発生槽1Oとの水位のバランスについて次のような問題点がある。   The hydrogen gas generator shown in FIG. 5 electrolyzes pure water using an ion exchange membrane. Since pure water is used, the apparatus does not deteriorate due to precipitation of impurities and the like. It is a long device. In addition, it is a small device that does not require large-scale equipment such as a circulation pump, and is suitable for use in general households. There are the following problems regarding the balance of the water level between the generation tank 1H and the oxygen gas generation tank 1O.

図5における電気分解板20は、樹脂製のリベット21を用いてイオン交換膜IEの両面に電極板2P、2Mを固定したものである。リベットで締結するには、リベットの頭部を半球形に変形させる加熱加工などが必要であるとともに、金属製の電極板にリベットの軸を通すための貫通孔を予め設ける必要があり、電気分解板20の製造に多くの時間とコストがかかる。   The electrolysis plate 20 in FIG. 5 is obtained by fixing electrode plates 2P and 2M on both surfaces of an ion exchange membrane IE using resin rivets 21. In order to fasten with rivets, it is necessary to heat the rivet head into a hemispherical shape, etc., and it is necessary to provide a through hole for passing the rivet shaft in the metal electrode plate in advance. It takes a lot of time and cost to manufacture the plate 20.

また、電気分解板20は、イオン交換膜IEを水素ガス発生槽1Hのケースと酸素ガス発生槽1Oのケースの間に挟み込んで電気分解槽1に固定され、両方のガス発生槽に水位差が生じると、水圧差でイオン交換膜IEが破損する恐れがある。図5の水素ガス発生装置では、酸素ガス発生槽1Oの上部に鋼球BLを用いた保圧弁が設置され、電気分解で生じた酸素ガスの大気中への開放を阻止して過剰な水位差の発生を抑えているが、鋼球BL及びその弁座VSの加工が複雑であるとともに、その開放圧力の設定が困難である。つまり、水素ガス発生槽1Hの圧力は、電気分解による水素ガスの発生量や洗浄ビン3からの水素ガスの抽出量により変動し、電気分解に伴って生じる熱による純水の蒸発量によっても変動する。そのため、例えば、鋼球BLの重さを変更しながら保圧弁の開放圧力を調整する作業は、作業者の熟練と時間を要するものとなる。
本発明の課題は、簡易な構造によって、リベットを用いずにイオン交換膜及び電極板を固定し、また、水素ガス発生槽と酸素ガス発生槽との間の水位差でイオン交換膜が破損しないようにして、上述の問題点を解決することにある。
The electrolysis plate 20 is fixed to the electrolysis tank 1 by sandwiching the ion exchange membrane IE between the case of the hydrogen gas generation tank 1H and the case of the oxygen gas generation tank 1O, and there is a difference in water level between both gas generation tanks. If it occurs, the ion exchange membrane IE may be damaged by the water pressure difference. In the hydrogen gas generator shown in FIG. 5, a pressure-holding valve using a steel ball BL is installed at the upper part of the oxygen gas generation tank 1O to prevent the oxygen gas generated by electrolysis from being released into the atmosphere and an excessive water level difference. However, the processing of the steel ball BL and its valve seat VS is complicated, and it is difficult to set the opening pressure. That is, the pressure in the hydrogen gas generation tank 1H varies depending on the amount of hydrogen gas generated by electrolysis and the amount of hydrogen gas extracted from the cleaning bottle 3, and also varies depending on the evaporation amount of pure water due to heat generated by electrolysis. To do. Therefore, for example, the operation of adjusting the opening pressure of the pressure holding valve while changing the weight of the steel ball BL requires the skill and time of the operator.
The object of the present invention is to fix the ion exchange membrane and the electrode plate without using rivets by a simple structure, and the ion exchange membrane is not damaged by the water level difference between the hydrogen gas generation tank and the oxygen gas generation tank. In this way, the above-mentioned problems are solved.

上記の課題に鑑み、本発明は、イオン交換膜を用いて水を電気分解し水素ガスを発生させる水素ガス発生装置において、イオン交換膜とその両面にそれぞれ設置される電極板とを、酸素ガス発生槽のケースと水素ガス発生槽のケースとの間に挟み、両方のケースを締め付けて密着した状態で保持し、リベット等の締結具を用いることなく電気分解槽に固定するものである。すなわち、本発明は
「イオン交換膜により仕切られた電気分解槽に水を貯留し、前記イオン交換膜の両面にそれぞれ設置した陽極電極及び陰極電極の間に直流電圧を印加して水の電気分解を行い、陰極電極から水素ガスを発生させる水素ガス発生装置であって、
前記電気分解槽は、前記イオン交換膜により、陽極電極側の酸素ガス発生槽と陰極電極側の水素ガス発生槽とに分割され、前記酸素ガス発生槽と前記水素ガス発生槽とがそれぞれ水を貯留するケースを備えるとともに、前記陽極電極と陰極電極とがそれぞれ板状の電極板として構成され
前記酸素ガス発生槽の上部が常時大気中に開放され、かつ、前記酸素ガス発生槽の底部と前記水素ガス発生槽の底部が水位調整用開閉弁を備えた連通管で連結されていて、前記水位調整用開閉弁は、陽極電極及び陰極電極に直流電圧が印加されて電気分解が行われるときは閉弁し、電気分解が終了したときは所定時間開弁して前記酸素ガス発生槽と前記水素ガス発生槽の水位が同一となるよう制御されており、さらに、
前記イオン交換膜とその両面にそれぞれ設置された前記電極板とは、それらを締結するリベットを用いることなく、前記酸素ガス発生槽のケースと前記水素ガス発生槽のケースとに挟まれて密着して保持される」
ことを特徴とする水素ガス発生装置となっている。
In view of the above problems, the present invention provides a hydrogen gas generator that electrolyzes water using an ion exchange membrane to generate hydrogen gas, and includes an ion exchange membrane and electrode plates respectively installed on both sides thereof. It is sandwiched between the case of the generation tank and the case of the hydrogen gas generation tank, both cases are clamped and held in close contact, and fixed to the electrolysis tank without using fasteners such as rivets. In other words, the present invention “retains water in an electrolysis tank partitioned by an ion exchange membrane and applies a DC voltage between the anode electrode and the cathode electrode respectively installed on both surfaces of the ion exchange membrane to electrolyze the water. A hydrogen gas generator for generating hydrogen gas from the cathode electrode,
The electrolysis tank is divided into an oxygen gas generation tank on the anode electrode side and a hydrogen gas generation tank on the cathode electrode side by the ion exchange membrane, and each of the oxygen gas generation tank and the hydrogen gas generation tank supplies water. With a case for storing, the anode electrode and the cathode electrode are each configured as a plate-like electrode plate ,
The upper part of the oxygen gas generation tank is always open to the atmosphere, and the bottom of the oxygen gas generation tank and the bottom of the hydrogen gas generation tank are connected by a communication pipe provided with a water level adjusting on-off valve, The water level adjusting on-off valve is closed when a direct current voltage is applied to the anode electrode and the cathode electrode and electrolysis is performed, and when electrolysis is completed, the valve is opened for a predetermined time and the oxygen gas generating tank and the The water level of the hydrogen gas generation tank is controlled to be the same, and
The ion exchange membrane and the electrode plates installed on both sides thereof are in close contact with each other between the case of the oxygen gas generation tank and the case of the hydrogen gas generation tank without using rivets for fastening them. Is retained "
This is a hydrogen gas generator characterized by this.

請求項2に記載のように、前記酸素ガス発生槽と前記水素ガス発生槽とのケースに、水を貯留し、前記イオン交換膜側の開放された空間部を設け、前記空間部の外側には平面を形成するとともに、前記空間部の周縁には、前記平面との間に段差を有し前記電極板を前記イオン交換膜に押圧する押圧部を形成することが好ましい。この場合においては、請求項3に記載のように、前記イオン交換膜に向けて直線状に延びるリブを前記空間部の周縁及び中央に設け、このリブを前記押圧部とすることができる。   As described in claim 2, in the case of the oxygen gas generation tank and the hydrogen gas generation tank, water is stored, an open space part on the ion exchange membrane side is provided, and the outside of the space part is provided. It is preferable to form a flat surface and at the periphery of the space portion, a pressing portion that has a step between the flat surface and presses the electrode plate against the ion exchange membrane. In this case, as described in claim 3, ribs extending linearly toward the ion exchange membrane are provided at the periphery and the center of the space portion, and the rib can be used as the pressing portion.

請求項4に記載のように、前記酸素ガス発生槽と前記水素ガス発生槽とのケースには、前記イオン交換膜と反対側に、それぞれ金属製の放熱板を設けることが好ましい。   According to a fourth aspect of the present invention, it is preferable that a metal heat dissipating plate is provided on the opposite side of the ion exchange membrane in the case of the oxygen gas generation tank and the hydrogen gas generation tank.

本発明の水素ガス発生装置は、イオン交換膜により仕切られた電気分解槽に水を入れ、イオン交換膜の両面に取り付けた一対の電極間に電流を流して水の電気分解を行い、陰極電極から水素ガスを発生させるものである。イオン交換膜を用いた小型の装置であって、電気分解する水として純水を使用できるため、耐用年数も長い。
そして、本発明の水素ガス発生装置では、酸素ガス発生槽と水素ガス発生槽とが水を貯留するケースを備えるとともに、イオン交換膜とその両面にそれぞれ設置された板状の電極板とが、酸素ガス発生槽のケースと水素ガス発生槽のケースとに挟まれて密着して保持される。単にケースを締め付けるだけで保持することができ、リベットのような締結具を使用する保持方法ではないので、電気分解槽の製造が非常に容易となる。
The hydrogen gas generator according to the present invention performs water electrolysis by flowing water between a pair of electrodes attached to both surfaces of an ion exchange membrane by putting water in an electrolysis tank partitioned by an ion exchange membrane, From which hydrogen gas is generated. This is a small device using an ion exchange membrane, and since pure water can be used as electrolyzed water, it has a long service life.
And in the hydrogen gas generation device of the present invention, the oxygen gas generation tank and the hydrogen gas generation tank have a case for storing water, and the ion-exchange membrane and the plate-like electrode plates respectively installed on both surfaces thereof, The oxygen gas generation tank case and the hydrogen gas generation tank case are sandwiched and held in close contact. It can be held simply by tightening the case, and since it is not a holding method using a fastener such as a rivet, the production of the electrolysis tank becomes very easy.

また、本発明の水素ガス発生装置では、イオン交換膜が、両側から金属製の電極板に挟まれ電極板と重なった状態で両方のケースの間に支持される。水素ガス発生装置の稼働中には、電気泳動などに伴って酸素ガス発生槽と水素ガス発生槽との間に水位差が生じ、イオン交換膜に水圧差が作用するが、本発明のイオン交換膜は、電極板により両面から支持され補強されるため、水圧差が作用しても破損することはない。
さらに、本発明では、酸素ガス発生槽の上部を常時大気中に開放し、かつ、酸素ガス発生槽の底部と水素ガス発生槽の底部とを水位調整用開閉弁を備えた連通管で連結し、その水位調整用開閉弁を、陽極電極及び陰極電極に直流電圧が印加されて電気分解が行われるときは閉弁し、電気分解が終了したときは、酸素ガス発生槽と水素ガス発生槽の水位が同一となるよう所定時間開弁している。
この水位調整用開閉弁を設置する構成によって、水素ガス発生装置の稼働中に生じた水位差は、電気分解が終了したときに簡単に解消できることとなる。つまり、イオン交換膜に作用する水圧差が、電気分解が終了したときの水位調整用開閉弁の開弁という簡易な制御手段によって確実に解消できる。図5の水素ガス発生装置のように、酸素ガス発生槽に鋼球を用いた保圧弁を設置するものではないので、鋼球や弁座等が不要で構造及び加工が簡易化され、保圧弁の開放圧力を調整する面倒な作業も必要としない
In the hydrogen gas generator of the present invention, the ion exchange membrane is supported between both cases while being sandwiched between metal electrode plates from both sides and overlapping the electrode plates. During operation of the hydrogen gas generator, a water level difference occurs between the oxygen gas generation tank and the hydrogen gas generation tank due to electrophoresis and the like, and a water pressure difference acts on the ion exchange membrane. Since the membrane is supported and reinforced from both sides by the electrode plate, it is not damaged even if a hydraulic pressure difference acts.
Further, in the present invention, the upper part of the oxygen gas generation tank is always open to the atmosphere, and the bottom part of the oxygen gas generation tank and the bottom part of the hydrogen gas generation tank are connected by a communication pipe provided with a water level adjusting on-off valve. The on / off valve for adjusting the water level is closed when a direct current voltage is applied to the anode electrode and the cathode electrode and electrolysis is performed, and when the electrolysis is completed, the oxygen gas generation tank and the hydrogen gas generation tank are closed. The valve is opened for a predetermined time so that the water level is the same.
With the configuration in which the water level adjusting on-off valve is installed, the water level difference generated during operation of the hydrogen gas generator can be easily eliminated when the electrolysis is completed. That is, the water pressure difference acting on the ion exchange membrane can be reliably eliminated by simple control means of opening the water level adjusting on / off valve when the electrolysis is completed. Unlike the hydrogen gas generator shown in FIG. 5, a pressure holding valve using a steel ball is not installed in the oxygen gas generating tank, so that a steel ball, a valve seat, etc. are not required, and the structure and processing are simplified. The troublesome work of adjusting the opening pressure is not required .

請求項2の発明は、酸素ガス発生槽と水素ガス発生槽とのケースに、イオン交換膜側の開放された空間部を設けてここに水を貯留し、空間部の外側のケースには平面を形成するとともに、空間部の周縁には、その平面との間に段差を有し電極板をイオン交換膜に押圧する押圧部を形成するものである。空間部の外側の平面(イオン交換膜側のいわば合わせ面)と段差のある押圧部には、金属製の電極板が収容されるようになるので、電極板がケースに対して確実に位置決めされ、イオン交換膜と両側の電極板とを強固に密着させて一体化することができる。
この場合に、請求項3の発明のように、水を貯留する空間部に、押圧部として、イオン交換膜に向けて直線状に延びるリブを周縁及び中央に設けたときは、空間部の周縁のみならず中央においてもイオン交換膜と電極板とが確実に密着し、電気分解中の通電の際の接触抵抗が低減することとなる。
In the invention of claim 2, the oxygen gas generation tank and the hydrogen gas generation tank are provided with a space portion opened on the ion exchange membrane side to store water, and the case outside the space portion is flat. In addition, a pressing portion that presses the electrode plate against the ion exchange membrane is formed on the periphery of the space portion with a step between the flat surface. Since the metal electrode plate is accommodated in the pressing portion having a step with the flat surface outside the space (so-called mating surface on the ion exchange membrane side), the electrode plate is securely positioned with respect to the case. In addition, the ion exchange membrane and the electrode plates on both sides can be firmly adhered and integrated.
In this case, as in the invention of claim 3, when ribs extending linearly toward the ion exchange membrane are provided as the pressing portion in the space portion for storing water at the periphery and the center, the periphery of the space portion Not only in the center, but also the ion exchange membrane and the electrode plate are securely adhered, and the contact resistance during energization during electrolysis is reduced.

請求項4の発明は、酸素ガス発生槽と水素ガス発生槽とのケースに、イオン交換膜と反対側にそれぞれ金属製の放熱板を設けるものである。このような放熱板を設けると、電気分解中に発生する熱を効率的に放熱し、温度上昇に起因する純水の蒸発や装置の熱的障害を回避できる。さらに、金属製の放熱板により酸素ガス発生槽等のケースの強度及び剛性が増加するため、ケースの合成樹脂等の壁の厚さを減少することが可能であって、ケース内の純水から放熱板への熱伝達における伝熱抵抗を一層低減することができる。放熱板の材料としては、アルミニウム等、熱伝導率の大きい金属が好ましい。   According to a fourth aspect of the present invention, a metal heat dissipating plate is provided on the opposite side of the ion exchange membrane in the case of the oxygen gas generation tank and the hydrogen gas generation tank. By providing such a heat sink, heat generated during electrolysis can be efficiently radiated, and evaporation of pure water and thermal failure of the apparatus due to temperature rise can be avoided. Furthermore, since the strength and rigidity of the case such as the oxygen gas generation tank is increased by the metal heat sink, it is possible to reduce the wall thickness of the case such as the synthetic resin, and from the pure water in the case. The heat transfer resistance in heat transfer to the heat sink can be further reduced. As a material of the heat sink, a metal having high thermal conductivity such as aluminum is preferable.

本発明の水素ガス発生装置の一実施例を示す全体図である。1 is an overall view showing an embodiment of a hydrogen gas generator of the present invention. 図1の水素ガス発生装置の電気分解槽の構造図である。It is a structural diagram of the electrolysis tank of the hydrogen gas generator of FIG. 図1の水素ガス発生装置のケースを示す図である。It is a figure which shows the case of the hydrogen gas generator of FIG. 図1の水素ガス発生装置の水位変化を表すグラフである。It is a graph showing the water level change of the hydrogen gas generator of FIG. 従来の水素ガス発生装置の一例を示す全体図である。It is a general view which shows an example of the conventional hydrogen gas generator.

以下、図面に基づいて、本発明の水素ガス発生装置について説明する。
図1は、図5と同様に、本発明の水素ガス発生装置を概略的に示す全体図であり、図1では、図5の水素ガス発生装置の部品と対応するものについては、同一の符号を付している。図2には、本発明の水素ガス発生装置における電気分解槽の具体的な構造を斜視図等で示し、また、図3は、電気分解槽のケースの構造を示す図となっている。
Hereinafter, the hydrogen gas generator of the present invention will be described with reference to the drawings.
FIG. 1 is an overall view schematically showing a hydrogen gas generator according to the present invention, as in FIG. 5. In FIG. 1, components corresponding to the parts of the hydrogen gas generator of FIG. Is attached. FIG. 2 is a perspective view showing the specific structure of the electrolysis tank in the hydrogen gas generator of the present invention, and FIG. 3 is a diagram showing the structure of the case of the electrolysis tank.

始めに、本発明の水素発生装置の全体的な構造について述べる。図1において、水を電気分解するための電気分解槽1の中間部には、イオン交換膜IEが設置されており、電気分解槽1は、水素ガス発生槽1Hと酸素ガス発生槽1Oとに分割されている。電気分解槽1に純水を供給するよう、電気分解槽1と並列に給水タンク5が設置され、給水タンク5の底部を、水素ガス発生槽1Hの底部と酸素ガス発生槽1Oの底部とに連結する連結管51が設けられる。   First, the overall structure of the hydrogen generator of the present invention will be described. In FIG. 1, an ion exchange membrane IE is installed at an intermediate portion of an electrolysis tank 1 for electrolyzing water, and the electrolysis tank 1 is divided into a hydrogen gas generation tank 1H and an oxygen gas generation tank 1O. It is divided. A water supply tank 5 is installed in parallel with the electrolysis tank 1 so as to supply pure water to the electrolysis tank 1, and the bottom of the water supply tank 5 is connected to the bottom of the hydrogen gas generation tank 1H and the bottom of the oxygen gas generation tank 1O. A connecting pipe 51 to be connected is provided.

一対の電極板2P、2Mが、イオン交換膜IEの両側にそれぞれ密着するように配置してあり、水素ガス発生槽1H側の電極板2Mが直流電源の−側に、酸素ガス発生槽1O側の電極板2Pが直流電源の+側に接続される。図2から分かるとおり、イオン交換膜IEと電極板2P、2Mとは、一体に重ね合わせた状態で、水素ガス発生槽1Hと酸素ガス発生槽1Oのケースの周縁部などに挟み込まれて保持される。電気分解槽1の詳細な構造については、図2、図3を参照しながら後述する。   A pair of electrode plates 2P and 2M are arranged so as to be in close contact with both sides of the ion exchange membrane IE, and the electrode plate 2M on the hydrogen gas generation tank 1H side is on the negative side of the DC power source and on the oxygen gas generation tank 1O side. The electrode plate 2P is connected to the + side of the DC power source. As can be seen from FIG. 2, the ion exchange membrane IE and the electrode plates 2 </ b> P and 2 </ b> M are sandwiched and held between the peripheral portions of the cases of the hydrogen gas generation tank 1 </ b> H and the oxygen gas generation tank 1 </ b> O in a state where they are integrally overlapped. The The detailed structure of the electrolysis tank 1 will be described later with reference to FIGS.

水素ガス発生槽1Hのケース1HCの上部には、水素ガス取出し筒1HEが立設され、電気分解により生じた水素ガスは、水素ガス取出し管PH(実際には水素ガス取出し筒1HEの横方向に接続される)を経由して、洗浄ビン3に導かれる。洗浄ビン3には一定水位まで清浄な水などが貯留されており、水素ガスは、その底部付近で放出される。また、洗浄ビン3には空気ポンプAPが接続してあり、電気分解で生じた水素ガスは、空気と混合されて抽出管4から目的の使用個所に送出される。図1の実施例では、空気ポンプAPからの空気は水中に放出されているが、水面から上方で放出してもよい。
なお、洗浄ビン3と連結する水素ガス取出し管PHの管路は、逆止弁CVが介在する分岐管路により大気と連通されている。逆止弁CVは、電気分解の終了により水素ガス発生槽1Hが冷却されて負圧となったときに、分岐管路から大気を導入して、洗浄ビン3内の浄水などが水素ガス発生槽1Hに逆流するのを防止する。
A hydrogen gas take-out cylinder 1HE is erected on the upper part of the case 1HC of the hydrogen gas generation tank 1H, and the hydrogen gas generated by the electrolysis is transferred to the hydrogen gas take-out pipe PH (actually in the lateral direction of the hydrogen gas take-out cylinder 1HE). To the cleaning bottle 3 via The cleaning bottle 3 stores clean water or the like up to a certain water level, and hydrogen gas is released near the bottom. In addition, an air pump AP is connected to the cleaning bottle 3, and hydrogen gas generated by electrolysis is mixed with air and sent from the extraction pipe 4 to a target use location. In the embodiment of FIG. 1, the air from the air pump AP is released into the water, but may be released upward from the water surface.
Note that the pipe of the hydrogen gas take-out pipe PH connected to the cleaning bottle 3 is communicated with the atmosphere by a branch pipe through which a check valve CV is interposed. When the hydrogen gas generation tank 1H is cooled to a negative pressure due to the end of electrolysis, the check valve CV introduces air from the branch pipe, and purified water in the cleaning bottle 3 is used as a hydrogen gas generation tank. Prevent backflow to 1H.

本発明の水素ガス発生装置においては、電気分解により生じた酸素ガスは常時大気中に放出されており、そのための放出筒1OEが、酸素ガス発生槽1Oのケース1OCの上部に立設されている。放出筒1OEは、所定の長さを備えた単なるパイプであるが、電気分解に伴う熱により酸素ガス発生槽1Oから発生する水蒸気が酸素ガス放出管1OEの内壁に凝結する。凝結し液化した水は、放出筒1OEから酸素ガス発生槽1O内に落下するので、純水の無駄な消費が抑止されるとともに、水蒸気が装置の他の部分で凝縮して不具合を起こすなどの事態が回避される。   In the hydrogen gas generation apparatus of the present invention, oxygen gas generated by electrolysis is always released into the atmosphere, and a discharge cylinder 1OE for the oxygen gas generation tank 1O is provided upright above the case 1OC of the oxygen gas generation tank 1O. . The discharge cylinder 1OE is a simple pipe having a predetermined length, but water vapor generated from the oxygen gas generation tank 1O condenses on the inner wall of the oxygen gas discharge pipe 1OE due to heat accompanying electrolysis. Condensed and liquefied water falls from the discharge cylinder 1OE into the oxygen gas generation tank 1O, so that wasteful consumption of pure water is suppressed and water vapor is condensed in other parts of the apparatus, causing problems. The situation is avoided.

さらに、本発明の水素ガス発生装置では、酸素ガス発生槽1Oの底部と水素ガス発生槽1Hの底部とが、水位調整用開閉弁SV1(電磁弁)の設置された連通管で連結される。この連通管は、図1の実施例の水素ガス発生装置では、給水タンク5の底部を、水素ガス発生槽1Hの底部と酸素ガス発生槽1Oの底部とに連結する連結管51の一部となっている。水位調整用開閉弁SV1は、電極板2P、2Mの間に直流電圧が印加されて電気分解が行われるとき、つまり、水素ガス発生装置の稼働中には閉鎖される。
水位調整用開閉弁SV1が水素ガス発生装置の稼働中に閉鎖されるため、電気分解中に発生する水素ガスの圧力(洗浄ビン3の水中への放出による背圧)が酸素ガス発生槽1Oに及ぶことはない。したがって、酸素ガス発生槽1Oが大気開放されていても、その中の純水が溢れだすことは防止される。
Furthermore, in the hydrogen gas generation apparatus of the present invention, the bottom of the oxygen gas generation tank 1O and the bottom of the hydrogen gas generation tank 1H are connected by a communication pipe provided with a water level adjusting on-off valve SV1 (electromagnetic valve). In the hydrogen gas generator of the embodiment of FIG. 1, this communication pipe is connected to a part of a connecting pipe 51 that connects the bottom of the water supply tank 5 to the bottom of the hydrogen gas generation tank 1H and the bottom of the oxygen gas generation tank 1O. It has become. The water level adjusting on-off valve SV1 is closed when a DC voltage is applied between the electrode plates 2P and 2M to perform electrolysis, that is, during operation of the hydrogen gas generator.
Since the water level adjusting on-off valve SV1 is closed during the operation of the hydrogen gas generator, the pressure of the hydrogen gas generated during electrolysis (the back pressure due to the discharge of the cleaning bottle 3 into the water) is applied to the oxygen gas generation tank 1O. Never reach. Therefore, even if the oxygen gas generation tank 1O is opened to the atmosphere, the pure water in the oxygen gas generation tank 1O is prevented from overflowing.

電気分解中には、電気泳動による水の移動あるいは熱による水の蒸発などに起因して、水素ガス発生槽1Hの水位と酸素ガス発生槽1Oの水位との間に差が生じる。この水位差は、本発明では、電気分解が終了し水素ガス発生装置の稼働が停止したときに、水位調整用開閉弁SV1を所定時間開弁することによって解消される。
電気分解中に生じる水位差は、水素ガス発生装置の通常の稼働時間であればそれほど大きな値とはならない。この水位差について本出願人が実験した結果を図4に示すが、水素ガス発生装置を2時間稼働(イオン交換膜を流れる電流:1.5A)した後の水位差は約20mmであり、稼働開始時に水素ガス発生槽1Hの上方に適当な空間を残すよう純水を充填すると、稼働中の水素ガス発生槽1Hからの溢れを防止することができる。そして、本発明のイオン交換膜IEは、電極板2P、2Mにより補強される形で固定されるので、電気分解中に生じる水位差で破損することはない。
During electrolysis, a difference occurs between the water level of the hydrogen gas generation tank 1H and the water level of the oxygen gas generation tank 1O due to movement of water by electrophoresis or evaporation of water by heat. In the present invention, this water level difference is eliminated by opening the water level adjusting on-off valve SV1 for a predetermined time when the electrolysis is completed and the operation of the hydrogen gas generator is stopped.
The difference in water level generated during electrolysis is not so large as long as it is a normal operation time of the hydrogen gas generator. FIG. 4 shows the result of the experiment conducted by the present applicant on this water level difference. The water level difference after the hydrogen gas generator was operated for 2 hours (current flowing through the ion exchange membrane: 1.5 A) was about 20 mm. When pure water is filled to leave an appropriate space above the hydrogen gas generation tank 1H at the start, overflow from the operating hydrogen gas generation tank 1H can be prevented. And since the ion exchange membrane IE of this invention is fixed in the form reinforced with the electrode plates 2P and 2M, it is not damaged by the water level difference produced during electrolysis.

図1に示す本発明の水素ガス発生装置の実施例においては、電気分解槽1と連なる給水タンク5の上部を、開放用開閉弁SV2(電磁弁)を介して大気と連通するとともに、水素ガス発生槽1Hの上部を、開放用開閉弁SV3(電磁弁)を介して大気と連通している。そして、これらの開放用開閉弁SV2、SV3を、水位調整用開閉弁SV1の開閉に合わせ、水位調整用開閉弁SV1が閉弁するときには閉弁し、開弁するときには開弁するよう制御する。これによって、稼働停止時に水位調整用開閉弁SV1を開放したときには、給水タンク5及び水素ガス発生槽1Hの上部も大気と連通するので、水位調整用開閉弁SV1の流路が小径であったとしても、給水タンク5、水素ガス発生槽1H及び酸素ガス発生槽1Oの水位が短時間で同一となる。   In the embodiment of the hydrogen gas generator of the present invention shown in FIG. 1, the upper portion of the water supply tank 5 connected to the electrolysis tank 1 is communicated with the atmosphere via an opening / closing valve SV2 (solenoid valve), and the hydrogen gas The upper part of the generation tank 1H is communicated with the atmosphere via an open / close valve SV3 (solenoid valve). The opening / closing valves SV2 and SV3 are controlled so as to be opened and closed when the water level adjusting on / off valve SV1 is closed and opened when the water level adjusting on / off valve SV1 is opened. As a result, when the water level adjustment on / off valve SV1 is opened when the operation is stopped, the upper part of the water supply tank 5 and the hydrogen gas generation tank 1H are also communicated with the atmosphere, so that the flow path of the water level adjustment on / off valve SV1 has a small diameter. In addition, the water levels of the water supply tank 5, the hydrogen gas generation tank 1H, and the oxygen gas generation tank 1O become the same in a short time.

また、図1に示す本発明の水素ガス発生装置の実施例では、洗浄ビン3に空気ポンプAPによる空気の供給装置を取り付け、水素ガス発生装置の稼働中においては、水素ガス発生槽1Hから導かれた水素ガスに空気を混合する。この構成によって、水素ガスの濃度は可燃範囲外の約3%まで希釈され、水素ガスの爆発の恐れが解消される。   Further, in the embodiment of the hydrogen gas generator of the present invention shown in FIG. 1, an air supply device by an air pump AP is attached to the cleaning bottle 3, and the hydrogen gas generator 1 is introduced from the hydrogen gas generator 1H during operation of the hydrogen gas generator. Air is mixed with the hydrogen gas. With this configuration, the concentration of hydrogen gas is diluted to about 3% outside the flammable range, and the risk of hydrogen gas explosion is eliminated.

ここで、本発明の水素ガス発生装置の図1の実施例における電気分解槽1の詳細な構造について、主に図2及び図3を参照して説明する。
図2に示すように、電気分解槽1は、中央に設置したイオン交換膜IEの両側に一対の電極板2P、2Mを配置し、これらを、水素ガス発生槽1Hのケース1HCと酸素ガス発生槽1Oのケース1OCの周縁部などで一体的に挟み込んだ基本的な構造を備えている。電極板の拡大図に示すとおり、この実施例における電極板2P、2Mは、エキスパンドメタル等をプレス成型して製造した網目板2Bに電極ケーブル2Cを溶接したものであって、網目板2Bの表面には、腐食防止のための白金のコーティングが施される。イオン交換膜IEは電極板2P、2Mよりも広く、重ね合わせたときに電極板の外側となる周辺部を備えている。
Here, the detailed structure of the electrolysis tank 1 in the embodiment of FIG. 1 of the hydrogen gas generator of the present invention will be described mainly with reference to FIGS.
As shown in FIG. 2, the electrolysis tank 1 has a pair of electrode plates 2P and 2M arranged on both sides of an ion exchange membrane IE installed in the center, and these are connected to a case 1HC of a hydrogen gas generation tank 1H and oxygen gas generation. It has a basic structure that is sandwiched integrally by the peripheral edge of the case 1OC of the tank 1O. As shown in the enlarged view of the electrode plate, the electrode plates 2P and 2M in this example are obtained by welding an electrode cable 2C to a mesh plate 2B manufactured by press molding expanded metal or the like, and the surface of the mesh plate 2B. Is coated with platinum to prevent corrosion. The ion exchange membrane IE is wider than the electrode plates 2P and 2M, and includes a peripheral portion that becomes the outside of the electrode plate when they are overlapped.

水素ガス発生槽1Hのケース1HCは、図3に詳しく示すとおり、一定の厚さを有する長方形断面の板状材に、その片面に開口する同じく長方形断面の空間部SPを設けたものであって、空間部の外側には、枠状の平面PLが形成される。空間部SPの開口部は、イオン交換膜IEにより閉鎖されて、長方形断面の空間部SPには電気分解用の純水が貯留される。酸素ガス発生槽1Oのケース1OCは、水素ガス発生槽のケース1HCと対称的な形状を備えており、両方のケースは、枠状の平面PLにイオン交換膜IEの周辺部を挟んで、背中合わせの形で結合される。結合する際には、イオン交換膜IEの合わせ面からの水の漏洩を防止するようOリングSLを設置する(A−A断面図参照)。そのため、酸素ガス発生槽1Oのケース1OCには、OリングSLの設置用の溝Gが形成してある。
これらのケースは、電気分解によるガスの発生状況を確認するため、例えば、透明な合成樹脂であるアクリル樹脂で製造するのが好ましい。
As shown in detail in FIG. 3, the case 1 HC of the hydrogen gas generation tank 1 </ b> H is obtained by providing a rectangular cross-section plate material having a certain thickness with a space SP having the same rectangular cross-section opening on one side. A frame-shaped plane PL is formed outside the space portion. The opening of the space SP is closed by the ion exchange membrane IE, and pure water for electrolysis is stored in the space SP having a rectangular cross section. The case 1OC of the oxygen gas generation tank 1O has a symmetrical shape with the case 1HC of the hydrogen gas generation tank, and both cases are back-to-back with the periphery of the ion exchange membrane IE sandwiched between the frame-shaped plane PL. Combined in the form of At the time of coupling, an O-ring SL is installed so as to prevent water leakage from the mating surface of the ion exchange membrane IE (see AA sectional view). Therefore, a groove G for installing the O-ring SL is formed in the case 1OC of the oxygen gas generation tank 1O.
These cases are preferably made of, for example, an acrylic resin, which is a transparent synthetic resin, in order to confirm the state of gas generation by electrolysis.

水素ガス発生槽1Hのケース1HCには、長方形断面の空間部SPの周縁部に、厚さ方向に直線状に延びる6本のリブ(突起)RBが設けられ、また、中央部分にも2本のリブRB(縦方向のリブで連結される)が設けられている。これらのリブRBは、ケース1HCと一体に形成されていて、リブRBの開口部側の端面は、ケース1HCの枠状の平面PLよりも僅かに引き込まれた位置に設定され(段差X)、この段差部分には、陰極側となる電極板2Mが収容される。酸素ガス発生槽1Oのケース1OCにも、同様なリブRBが一体に形成されている。   The case 1HC of the hydrogen gas generation tank 1H is provided with six ribs (protrusions) RB extending linearly in the thickness direction at the periphery of the rectangular space SP, and two at the center. Ribs RB (connected by longitudinal ribs). These ribs RB are formed integrally with the case 1HC, and the end surface on the opening side of the rib RB is set at a position slightly pulled in from the frame-shaped plane PL of the case 1HC (step X). The stepped portion accommodates the electrode plate 2M on the cathode side. A similar rib RB is also integrally formed in the case 1OC of the oxygen gas generation tank 1O.

図2に示すとおり、イオン交換膜IEの両側に電極板2P、2Mを配置し、これらを、水素ガス発生槽1Hのケース1HCと酸素ガス発生槽1Oのケース1OCで挟み込んだときは、イオン交換膜IEの周辺部が両方のケースの枠状の平面PLに挟まれて固定されると同時に、電極板2P、2Mの網目板2B部分が、リブRBの開口部側の端面とケースの枠状の平面PLとの段差Xにそれぞれ入り込み、リブRBでイオン交換膜IEに押し付けられる。このように、リブRBは、電極板2P、2Mをイオン交換膜IEに押圧する押圧部として機能し、本発明の電気分解槽1では、水素ガス発生槽1Hのケース1HCと酸素ガス発生槽1Oのケース1OCを単に締め付けることにより、イオン交換膜IEの両側に電極板2P、2Mを強固に密着させることができる(A−A断面図参照)。   As shown in FIG. 2, when the electrode plates 2P and 2M are arranged on both sides of the ion exchange membrane IE and are sandwiched between the case 1HC of the hydrogen gas generation tank 1H and the case 1OC of the oxygen gas generation tank 1O, ion exchange is performed. The peripheral portion of the film IE is sandwiched and fixed between the frame-shaped planes PL of both cases, and at the same time, the mesh plate 2B portion of the electrode plates 2P and 2M is formed between the end face of the opening side of the rib RB and the frame shape of the case. Each of them enters a step X with respect to the plane PL, and is pressed against the ion exchange membrane IE by the rib RB. As described above, the rib RB functions as a pressing portion that presses the electrode plates 2P and 2M against the ion exchange membrane IE. In the electrolysis tank 1 of the present invention, the case 1HC and the oxygen gas generation tank 1O of the hydrogen gas generation tank 1H. By simply tightening the case 1OC, the electrode plates 2P and 2M can be firmly adhered to both sides of the ion exchange membrane IE (see the AA sectional view).

つまり、本発明の電気分解槽1では、締結具を用いないので、網目状の電極板に孔を開ける煩雑な作業を省くことができ、また、孔開けに伴って生じやすい不具合、例えば、いわゆる「バリ」によるイオン交換膜IEの破損、を避けることができる。
なお、図2、図3の実施例では、ケース1HC等の厚さ方向に直線状に延びるリブRBを設けて押圧部としているが、枠状の平面PLとの間に段差Xを設定した棚状の突出部(ケースの厚さ方向の寸法は小さい)を、空間部SPの周縁部から横方向に突出させて押圧部としてもよい。
That is, in the electrolysis tank 1 of the present invention, since no fastener is used, a troublesome operation of making a hole in the mesh-like electrode plate can be omitted, and a problem that easily occurs with the opening, for example, so-called Damage to the ion exchange membrane IE due to “burrs” can be avoided.
2 and 3, the rib RB extending linearly in the thickness direction of the case 1HC and the like is provided as the pressing portion, but the shelf is set with a step X between the frame-shaped plane PL. A projecting portion (the dimension of the case in the thickness direction of the case is small) may be projected from the peripheral portion of the space portion SP in the lateral direction to be a pressing portion.

さらに、本発明の電気分解槽1では、図2に示すとおり、水素ガス発生槽1Hのケース1HCと酸素ガス発生槽1Oのケース1OCとの裏側(イオン交換膜IEと接する開口部の反対側)に、それぞれアルミニウム製の放熱板RDが設けられている。この放熱板RDは、ケース1HC、1OCと同一形状をなす板材の表面に、縦方向に延びる多数の放熱フィンRFを一体に形成したもので、ケース1HC等の裏側の壁W(図3)に密着して取り付けられる。   Furthermore, in the electrolysis tank 1 of the present invention, as shown in FIG. 2, the back side of the case 1HC of the hydrogen gas generation tank 1H and the case 1OC of the oxygen gas generation tank 1O (the opposite side of the opening in contact with the ion exchange membrane IE) Each is provided with a heat sink RD made of aluminum. The heat radiating plate RD is formed by integrally forming a number of heat radiating fins RF extending in the vertical direction on the surface of a plate material having the same shape as the cases 1HC and 1OC. Installed in close contact.

電気分解を利用する水素ガス発生装置では、電気分解に伴う発熱によって純水が蒸発するが、本発明では、その熱の大気中への放熱が放熱板RDによって促進され、電気分解槽1の温度上昇が抑制される。したがって、水素ガス発生装置における熱的障害を回避できるとともに、純水の無駄な消費も回避できる。
また、アルミニウム製の放熱板RDを水素ガス発生槽1Hのケース1HC等の裏側に取り付けることにより、アクリル樹脂製のケース1HC等が補強され、電気分解槽1の強度及び剛性が増加する。そのため、ケース1HC等の裏側の壁Wの厚さを小さくすることが可能となり、放熱板RDへの熱伝達が良好となる。イオン交換膜IEを挟んで対称的に配置される、水素ガス発生槽1Hのケース1HC及び放熱板RDと酸素ガス発生槽1Oのケース1OC及び放熱板RDとは、ケースの周縁部に設置した、全体を貫通する通しボルト等を用いて一体的に締結される(図2の組立図参照)。
In a hydrogen gas generator using electrolysis, pure water evaporates due to heat generated by electrolysis, but in the present invention, the heat radiation to the atmosphere is promoted by the radiator plate RD, and the temperature of the electrolysis tank 1 is increased. The rise is suppressed. Therefore, it is possible to avoid a thermal failure in the hydrogen gas generator and to avoid wasteful consumption of pure water.
Moreover, by attaching the heat sink RD made of aluminum to the back side of the case 1HC of the hydrogen gas generation tank 1H, the case 1HC made of acrylic resin is reinforced, and the strength and rigidity of the electrolysis tank 1 are increased. Therefore, the thickness of the wall W on the back side of the case 1HC and the like can be reduced, and heat transfer to the heat sink RD is improved. The case 1HC and the heat radiating plate RD of the hydrogen gas generating tank 1H and the case 1OC and the heat radiating plate RD of the oxygen gas generating tank 1O, which are arranged symmetrically with the ion exchange membrane IE interposed therebetween, are installed at the peripheral edge of the case. It is fastened integrally using a through bolt or the like penetrating the whole (see the assembly drawing in FIG. 2).

以上詳述したように、本発明は、イオン交換膜を用いて水を電気分解し水素ガスを発生させる水素ガス発生装置において、イオン交換膜とその両面にそれぞれ設置される電極板とを、酸素ガス発生槽のケースと水素ガス発生槽のケースとの間に挟み、両方のケースを締め付けて密着した状態で保持し、締結具を用いることなく電気分解槽に固定するものである。上述の実施例では、酸素ガス発生槽等のケースの材料として透明なアクリル樹脂を使用しているが、その他の樹脂等が使用できるのは言うまでもない。また、水位調整用開閉弁として、電磁弁に代えて空気圧により操作される開閉弁を用いるなど、上述の実施例に対し種々の変形が可能であるのは明らかである。   As described in detail above, the present invention relates to an ion exchange membrane and electrode plates installed on both sides thereof in an oxygen gas generator that generates hydrogen gas by electrolyzing water using an ion exchange membrane. It is sandwiched between the case of the gas generation tank and the case of the hydrogen gas generation tank, both cases are clamped and held in close contact, and are fixed to the electrolysis tank without using a fastener. In the above-described embodiment, a transparent acrylic resin is used as a material for a case such as an oxygen gas generation tank, but it goes without saying that other resins can be used. Further, it is apparent that various modifications can be made to the above-described embodiment, such as using an on-off valve operated by air pressure instead of an electromagnetic valve as the water level adjusting on-off valve.

1 電気分解槽
1H 水素ガス発生槽
1O 酸素ガス発生槽
2M、2P 電極板
3 洗浄ビン
5 給水タンク
IE イオン交換膜
RB リブ(押圧部)
RD 放熱板
DESCRIPTION OF SYMBOLS 1 Electrolysis tank 1H Hydrogen gas generation tank 1O Oxygen gas generation tank 2M, 2P Electrode plate 3 Washing bottle 5 Water supply tank IE Ion exchange membrane RB Rib (pressing part)
RD heat sink

Claims (4)

イオン交換膜により仕切られた電気分解槽に水を貯留し、前記イオン交換膜の両面にそれぞれ設置した陽極電極及び陰極電極の間に直流電圧を印加して水の電気分解を行い、陰極電極から水素ガスを発生させる水素ガス発生装置であって、
前記電気分解槽は、前記イオン交換膜により、陽極電極側の酸素ガス発生槽と陰極電極側の水素ガス発生槽とに分割され、前記酸素ガス発生槽と前記水素ガス発生槽とがそれぞれ水を貯留するケースを備えるとともに、前記陽極電極と陰極電極とがそれぞれ板状の電極板として構成され
前記酸素ガス発生槽の上部が常時大気中に開放され、かつ、前記酸素ガス発生槽の底部と前記水素ガス発生槽の底部が水位調整用開閉弁を備えた連通管で連結されていて、前記水位調整用開閉弁は、陽極電極及び陰極電極に直流電圧が印加されて電気分解が行われるときは閉弁し、電気分解が終了したときは所定時間開弁して前記酸素ガス発生槽と前記水素ガス発生槽の水位が同一となるよう制御されており、さらに、
前記イオン交換膜とその両面にそれぞれ設置された前記電極板とは、それらを締結するリベットを用いることなく、前記酸素ガス発生槽のケースと前記水素ガス発生槽のケースとに挟まれて密着して保持されることを特徴とする水素ガス発生装置。
Water is stored in an electrolysis tank partitioned by an ion exchange membrane, and electrolysis of the water is performed by applying a DC voltage between the anode electrode and the cathode electrode respectively installed on both surfaces of the ion exchange membrane. A hydrogen gas generator for generating hydrogen gas,
The electrolysis tank is divided into an oxygen gas generation tank on the anode electrode side and a hydrogen gas generation tank on the cathode electrode side by the ion exchange membrane, and each of the oxygen gas generation tank and the hydrogen gas generation tank supplies water. With a case for storing, the anode electrode and the cathode electrode are each configured as a plate-like electrode plate ,
The upper part of the oxygen gas generation tank is always open to the atmosphere, and the bottom of the oxygen gas generation tank and the bottom of the hydrogen gas generation tank are connected by a communication pipe provided with a water level adjusting on-off valve, The water level adjusting on-off valve is closed when a direct current voltage is applied to the anode electrode and the cathode electrode and electrolysis is performed, and when electrolysis is completed, the valve is opened for a predetermined time and the oxygen gas generating tank and the The water level of the hydrogen gas generation tank is controlled to be the same, and
The ion exchange membrane and the electrode plates installed on both sides thereof are in close contact with each other between the case of the oxygen gas generation tank and the case of the hydrogen gas generation tank without using rivets for fastening them. The hydrogen gas generator characterized by being held.
前記酸素ガス発生槽と前記水素ガス発生槽とのケースには、水を貯留し、前記イオン交換膜側の開放された空間部が設けられ、前記空間部の外側には平面が形成されるとともに、前記空間部の周縁には、前記平面との間に段差を有し前記電極板を前記イオン交換膜に押圧する押圧部が形成される請求項1に記載の水素ガス発生装置。 In the case of the oxygen gas generation tank and the hydrogen gas generation tank, water is stored, an open space part on the ion exchange membrane side is provided, and a flat surface is formed outside the space part. The hydrogen gas generator according to claim 1, wherein a pressing portion that has a step with respect to the plane and presses the electrode plate against the ion exchange membrane is formed at a peripheral edge of the space portion. 前記押圧部が、前記空間部の周縁及び中央に設けられ、前記イオン交換膜に向けて直線状に延びるリブである請求項2に記載の水素ガス発生装置。 The hydrogen gas generator according to claim 2, wherein the pressing portion is a rib provided at a peripheral edge and a center of the space portion and extending linearly toward the ion exchange membrane. 前記酸素ガス発生槽と前記水素ガス発生槽のケースには、前記イオン交換膜と反対側に、それぞれ金属製の放熱板が設けられる請求項1乃至請求項3のいずれかに記載の水素ガス発生装置。 The hydrogen gas generation according to any one of claims 1 to 3, wherein a metal heat dissipating plate is provided on a side opposite to the ion exchange membrane in the case of the oxygen gas generation tank and the hydrogen gas generation tank. apparatus.
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