JPH0978278A - Hydrogen/oxygen generating device - Google Patents

Hydrogen/oxygen generating device

Info

Publication number
JPH0978278A
JPH0978278A JP7233996A JP23399695A JPH0978278A JP H0978278 A JPH0978278 A JP H0978278A JP 7233996 A JP7233996 A JP 7233996A JP 23399695 A JP23399695 A JP 23399695A JP H0978278 A JPH0978278 A JP H0978278A
Authority
JP
Japan
Prior art keywords
pure water
water tank
hydrogen
water
makeup
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP7233996A
Other languages
Japanese (ja)
Other versions
JP3487687B2 (en
Inventor
Hiromichi Oda
博通 小田
Shinichi Yasui
信一 安井
Takashi Sasaki
隆 佐々木
Seiji Hirai
清司 平井
Mamoru Nagao
衛 長尾
Michiyuki Harada
宙幸 原田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Corp
Shinko Pantec Co Ltd
Original Assignee
Mitsubishi Corp
Shinko Pantec Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Corp, Shinko Pantec Co Ltd filed Critical Mitsubishi Corp
Priority to JP23399695A priority Critical patent/JP3487687B2/en
Publication of JPH0978278A publication Critical patent/JPH0978278A/en
Application granted granted Critical
Publication of JP3487687B2 publication Critical patent/JP3487687B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain high pressure high purity gaseous hydrogen and oxygen by replenishing a pure water in a pure water vessel provided with a hydrogen/ oxygen generator through a replenishing water tank from a pure water tank by the difference of altitude. SOLUTION: The hydrogen/oxygen generator 1 provided with a solid high molecular electrolyte film or the like is arranged in the pure water vessel 3 and gaseous hydrogen and oxygen are produced by electrolyzing the pure water. The replenishing water tank 14 is arranged at a higher position than that of the pure water vessel 3 and the pure water is replenished through a replenishing water passage 13 by utilizing the difference of the altitude while equalizing the pressure through a communicating passage 22. Further, the pure water tank 21 is arranged at the higher position than that of the replenishing tank 14 and the pure water is supplied to the replenishing water tank 14 through a pure water supply passage 20 from a water feed tank 21 in the state that a gas vent passage 15 is opened.

Description

【発明の詳細な説明】Detailed Description of the Invention

【０００１】[0001]

【発明の属する技術分野】本発明は、固体電解質膜を隔
膜として用い、陽極側に純水を供給しながら電気分解し
て、陽極側から酸素ガスを、陰極側から水素ガスを発生
させるための水素・酸素発生装置に関し、特に半導体製
造分野、原子力発電分野などにおいて必要とされる高純
度の水素ガス、酸素ガスを発生するための装置に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention uses a solid electrolyte membrane as a diaphragm for electrolyzing while supplying pure water to the anode side to generate oxygen gas from the anode side and hydrogen gas from the cathode side. The present invention relates to a hydrogen / oxygen generator, and more particularly to a device for generating high-purity hydrogen gas and oxygen gas required in the fields of semiconductor manufacturing, nuclear power generation, and the like.

【０００２】[0002]

【従来の技術】従来より、例えば、半導体製造工場など
水素ガス、酸素ガスを消費する工場では、固体高分子電
解質膜等の電解質膜を隔膜として用いて、陽極側と陰極
側とに分離して、純水を陽極側に供給しながら純水を電
気分解して、陽極側から酸素ガスを、陰極側から水素ガ
スをそれぞれ発生するように構成した水電解セルからな
る水素・酸素発生装置を設置することが行われている。2. Description of the Related Art Conventionally, for example, in a factory that consumes hydrogen gas and oxygen gas such as a semiconductor manufacturing factory, an electrolyte membrane such as a solid polymer electrolyte membrane is used as a diaphragm to separate the anode side and the cathode side. Install a hydrogen / oxygen generator consisting of a water electrolysis cell configured to electrolyze pure water while supplying pure water to the anode side to generate oxygen gas from the anode side and hydrogen gas from the cathode side. Is being done.

【０００３】このような水素・酸素発生装置では、その
発生ガス圧力が低いために、発生したガスをコンプレッ
サーなどのガス圧縮機を用いて加圧して使用する必要が
あるが、圧縮機の潤滑オイル等による不純物が混入する
おそれがあり、そのため、高純度の水素ガス、酸素ガス
を必要とする半導体製造分野においては好ましくなかっ
た。In such a hydrogen / oxygen generator, since the generated gas pressure is low, it is necessary to pressurize the generated gas using a gas compressor such as a compressor. Therefore, it is not preferable in the field of semiconductor manufacturing that requires high-purity hydrogen gas and oxygen gas.

【０００４】このコンプレッサーによる不純物の混入が
なく、高純度でしかも高圧の水素ガス、酸素ガスを供給
することの可能な水素・酸素発生装置として、純水を満
たした容器内に水電解セルを収納した構成の水素・酸素
発生装置が、特表昭63-502908 号「水の電気分解方法及
びその装置」、特公平1-247591号「水素製造装置」、特
開平6-33283 号「水素発生装置」に開示されている。As a hydrogen / oxygen generator capable of supplying high-purity and high-pressure hydrogen gas and oxygen gas without the inclusion of impurities by the compressor, a water electrolysis cell is housed in a container filled with pure water. A hydrogen / oxygen generator having the above-mentioned configuration is disclosed in Japanese Patent Publication No. 63-502908, "Electrolysis method of water and its device", Japanese Patent Publication No. 1-247591, "Hydrogen production device", and Japanese Patent Laid-Open No. 6-33283, "Hydrogen generator." ].

【０００５】また、本発明者等は、既に特願平7-24737
号「水素・酸素ガス発生装置」において、純水容器に水
電解セルを浸漬するとともに、その酸素ガス分離室及び
水素ガス気液分離室の水面とガス圧力を制御できるよう
にして、酸素側と水素側のガス圧力の差圧を所定の小さ
い値にするよに構成したものである。そして、これによ
り、水電解セルの陽極室と陰極室とを分離している固体
高分子電解質膜などの隔膜に作用する差圧を小さくで
き、隔膜の破損の防止、水電解セルのシール部からのガ
スの漏洩の防止が可能で、その結果発生ガス圧力を高く
することができる技術を開示した。Further, the present inventors have already filed Japanese Patent Application No. 7-24737.
In the No. “Hydrogen / oxygen gas generator”, the water electrolysis cell is immersed in a pure water container, and the water surface and gas pressure of the oxygen gas separation chamber and hydrogen gas gas-liquid separation chamber can be controlled so that the oxygen side The pressure difference of the gas pressure on the hydrogen side is set to a predetermined small value. And thereby, the pressure difference acting on the diaphragm such as the solid polymer electrolyte membrane separating the anode chamber and the cathode chamber of the water electrolysis cell can be reduced, the damage of the membrane can be prevented, and the sealing portion of the water electrolysis cell can be reduced. It has been disclosed a technique capable of preventing the leakage of the gas, and consequently increasing the generated gas pressure.

【０００６】[0006]

【発明が解決しようとする課題】ところで、このような
従来の水素・酸素発生装置に用いる水電解セルの構造と
しては、本発明者等が既に特開平5-287570号において、
図２に示したように、固体電解質128 、例えば、カチオ
ン交換膜（フッ素樹脂系スルフォン酸カチオン交換膜、
例えば、デュポン社製「ナフィオン117 」）の両面に白
金属族金属等からなる多孔質の陽極122 及び陰極123 を
接合した構造の固体高分子電解質膜121 を隔膜として用
いることで、陽極室124 と陰極室125 とに分離した構造
の水電解セル116 を形成し、該水電解セル116 の陽極室
124 に純水を供給しながら電気分解を行い、陽極室124
から酸素ガスを、陰極室125 から水素ガスをそれぞれ発
生するように構成したものである。すなわち、この場
合、水を陽極側に供給しながら電気分解することによ
り、陽極側では、2H2 O →O 2 ＋4H+ ＋4e- のような反
応が起こり酸素ガスが発生し、陰極側では、4H+ ＋4e-
→２H 2 の反応が起こり水素ガスが発生するものであ
る。By the way, as the structure of the water electrolysis cell used in such a conventional hydrogen / oxygen generator, the present inventors have already disclosed in JP-A-5-287570.
As shown in FIG. 2, the solid electrolyte 128, for example, a cation exchange membrane (a fluororesin sulfonic acid cation exchange membrane,
For example, by using a solid polymer electrolyte membrane 121 having a structure in which a porous anode 122 and a cathode 123 made of a white metal group metal or the like are bonded to both surfaces of DuPont “Nafion 117”) as a diaphragm, A water electrolysis cell 116 having a structure separated from the cathode chamber 125 is formed, and an anode chamber of the water electrolysis cell 116 is formed.
While supplying pure water to 124, electrolysis is performed and
Oxygen gas and hydrogen gas from the cathode chamber 125, respectively. That is, in this case, by electrolyzing while supplying water to the anode side, a reaction such as 2H 2 O → O 2 + 4H + + 4e − occurs on the anode side to generate oxygen gas, and on the cathode side, 4H + + 4e -
→ 2H 2 reaction occurs and hydrogen gas is generated.

【０００７】この場合、水電解セルを純水容器内に浸し
た構造であり、電気分解反応が進むにしたがって、純水
容器内の純水が消費されていくので、補充水を補充する
必要があるが、この場合、高圧で操業しているので、純
水容器内も10〜30kg/cm 2 程度の圧力を有するため、通
常は、純水補充タンクからの純水を高圧ポンプなどで予
め昇圧する必要がある。しかしながら、このように高圧
ポンプなどを用いた場合には、高圧ポンプなどの構成部
品の潤滑オイル等による不純物が混入するおそれがあ
り、そのため、高純度の水素ガス、酸素ガスを必要とす
る半導体製造分野においては好ましくなかった。In this case, the water electrolysis cell is soaked in a pure water container, and the pure water in the pure water container is consumed as the electrolysis reaction progresses. Therefore, it is necessary to supplement the replenishing water. However, in this case, since the operation is performed at a high pressure, the pressure in the pure water container also has a pressure of about 10 to 30 kg / cm 2. There is a need to. However, when a high-pressure pump or the like is used as described above, impurities such as lubricating oil of components such as the high-pressure pump may be mixed, and therefore, semiconductor manufacturing that requires high-purity hydrogen gas or oxygen gas. It was not favorable in the field.

【０００８】本発明は、このような実情を考慮して、構
成部品の潤滑オイル等による不純物が混入するおそれの
ある高圧ポンプなどの動力源を用いることなく、純水容
器内の高圧を維持したまま、純水容器内の純水のガス発
生に消費された純水を、補充水として容易に補充可能
で、しかも高圧、高純度の水素ガス、酸素ガスを得るこ
とのできる水素・酸素発生装置を提供することを目的と
する。In consideration of such circumstances, the present invention maintains the high pressure in the pure water container without using a power source such as a high pressure pump which may contain impurities such as lubricating oil of the components. As it is, the hydrogen / oxygen generator that can easily replenish the pure water consumed for generating the pure water gas in the pure water container as the replenishing water and can obtain the high-pressure, high-purity hydrogen gas and oxygen gas. The purpose is to provide.

【０００９】[0009]

【課題を解決するための手段】本発明は、前述したよう
な従来技術における課題及び目的を達成するために発明
なされたものであって、下記の（１）〜（４）を、その
構成要旨とするものである。The present invention has been made to achieve the problems and objects in the prior art as described above. The following (1) to (4) are summarized as follows. It is what

【００１０】（１）固体高分子電解質膜等の電解質膜を
隔膜として用いて、陽極側と陰極側とに分離して、純水
を陽極側に供給しながら純水を電気分解して、陽極側か
ら酸素ガスを、陰極側から水素ガスをそれぞれ発生する
ように構成され、且つ純水容器内に収容された水電解セ
ルを備えた水素・酸素発生器と、水素・酸素発生器の純
水容器内に純水を補給するために、水素・酸素発生器の
純水容器よりも高水平位置に配設され、且つ補給水経路
を介して水素・酸素発生器の純水容器に接続された補給
水タンクと、補給水タンク上方に配設されたガス抜き経
路と、補給水タンクに純水を供給するために、補給水タ
ンクよりも高水平位置に配設され、且つ純水供給経路を
介して補給水タンクに接続された純水タンクと、水素・
酸素発生器の純水容器上部と補給水タンクの上部を連通
する連通経路とから構成され、純水タンク、補給水タン
ク、及び純水容器の水位差によって、純水タンクから補
給水タンクを介して、水素・酸素発生器の純水容器内に
補給するように構成したことを特徴とする水素・酸素発
生装置。(1) An electrolyte membrane such as a solid polymer electrolyte membrane is used as a diaphragm to separate it into an anode side and a cathode side, and the pure water is electrolyzed while supplying the pure water to the anode side. Hydrogen / oxygen generator equipped with a water electrolysis cell that is configured to generate oxygen gas from the cathode side and hydrogen gas from the cathode side, and a pure water of the hydrogen / oxygen generator. In order to replenish the pure water in the container, it was placed at a higher horizontal position than the pure water container of the hydrogen / oxygen generator, and was connected to the pure water container of the hydrogen / oxygen generator through the makeup water path. A make-up water tank, a degassing path arranged above the make-up water tank, and a pure water supply path arranged at a higher horizontal position than the make-up water tank for supplying pure water to the make-up water tank. Pure water tank connected to the makeup water tank via
It consists of a communication path that connects the upper part of the pure water container of the oxygen generator and the upper part of the makeup water tank, and the pure water tank, the makeup water tank, and the makeup water tank via the makeup water tank depending on the water level difference of the pure water container. A hydrogen / oxygen generator characterized in that it is configured to be replenished in a pure water container of the hydrogen / oxygen generator.

【００１１】（２）水素・酸素発生器の純水容器には、
純水容器の液面位置を検出するための純水容器液面検知
装置が設けられており、純水容器液面検知装置によって
検知された純水容器液面位置が、予め設定されたレベル
より低い場合に、補給水経路及び連通経路を閉止した状
態で、純水供給経路及びガス抜き経路を開放して、純水
タンクと補給水タンクとの水位差によって、純水タンク
より補給水タンクに補給水を供給するように構成され、
補給水タンクには、補給水タンクの液面位置を検出する
ための補給水タンク液面検知装置が設けられており、補
給水タンク液面検知装置によって検知された補給水タン
ク液面位置が予め設定されたレベルよりも高い場合に、
純水供給経路及びガス抜き経路を閉止するとともに、連
通経路を開放して、補給水タンク内と水素・酸素発生器
の純水容器内を同圧力とするように構成され、補給水タ
ンク内と水素・酸素発生器の純水容器内が同圧力となっ
た後に、補給水経路を開放して、補給水タンクと水素・
酸素発生器の純水容器との水位差によって、補給水を補
給水タンクから純水容器に供給するように構成されてい
ることを特徴とする前述の（１）に記載の水素・酸素発
生装置。(2) In the pure water container of the hydrogen / oxygen generator,
A pure water container liquid level detection device for detecting the liquid level position of the pure water container is provided, and the pure water container liquid level position detected by the pure water container liquid level detection device is higher than a preset level. If it is low, open the pure water supply route and the degassing route with the makeup water route and the communication route closed, and change from the pure water tank to the makeup water tank due to the water level difference between the pure water tank and the makeup water tank. Configured to provide makeup water,
The makeup water tank is provided with a makeup water tank liquid level detection device for detecting the makeup level of the makeup water tank, and the makeup water tank liquid level position detected by the makeup water tank liquid level detection device is set in advance. If it is higher than the set level,
It is configured to close the pure water supply path and the degassing path and open the communication path so that the inside of the makeup water tank and the inside of the pure water container of the hydrogen / oxygen generator have the same pressure. After the pressure in the pure water container of the hydrogen / oxygen generator has reached the same pressure, the make-up water path is opened, and the make-up water tank and hydrogen
The hydrogen / oxygen generator according to the above (1), characterized in that makeup water is supplied from the makeup water tank to the pure water container by a water level difference between the oxygen generator and the pure water container. .

【００１２】（３）補給水タンク液面位置の予め設定さ
れたレベルが、満水レベルとなるように設定されている
ことを特徴とする前述の（２）に記載の水素・酸素発生
装置。(3) The hydrogen / oxygen generator according to the above (2), characterized in that the preset level of the liquid surface position of the makeup water tank is set to the full water level.

【００１３】（４）補給水経路、ガス抜き経路、純水供
給経路及び連通経路の開閉を、それぞれの経路に設けた
開閉弁によって行うように構成されていることを特徴と
する前述の（２）又は（３）に記載の水素・酸素発生装
置。(4) The makeup water path, the gas vent path, the pure water supply path, and the communication path are configured to be opened and closed by an on-off valve provided in each path. ) Or (3) hydrogen / oxygen generator.

【００１４】すなわち、本発明の水素・酸素発生装置で
は、純水容器液面位置が、予め設定されたレベルより低
い場合に、補給水経路及び連通経路を閉止した状態で、
純水供給経路及びガス抜き経路を開放して、純水タンク
と補給水タンクとの水位差によって、純水タンクより補
給水タンクに補給水が供給され、補給水タンク液面位置
が予め設定されたレベルよりも高い場合に、純水供給経
路及びガス抜き経路を閉止するとともに、連通経路を開
放して、補給水タンク内と水素・酸素発生器の純水容器
内を同圧力とし、補給水タンク内と水素・酸素発生器の
純水容器内を同圧力となった後に、補給水経路を開放し
て、補給水タンクと水素・酸素発生器の純水容器との水
位差によって、補給水を補給水タンクから純水容器に供
給するように構成されている。That is, in the hydrogen / oxygen generator of the present invention, when the liquid surface position of the pure water container is lower than a preset level, the makeup water passage and the communication passage are closed,
The pure water supply path and the degassing path are opened, and the make-up water is supplied from the pure water tank to the make-up water tank due to the water level difference between the pure water tank and the make-up water tank, and the make-up water tank liquid level position is preset. If the level is higher than the specified level, close the pure water supply path and degassing path, open the communication path, and make the pressure in the make-up water tank and the pure water container of the hydrogen / oxygen generator the same. After the tank and the deionized water container of the hydrogen / oxygen generator have the same pressure, the make-up water path is opened, and the make-up water is supplied due to the water level difference between the make-up water tank and the deionized water container of the hydrogen / oxygen generator. Is supplied from the makeup water tank to the pure water container.

【００１５】[0015]

【発明の実施の形態】以下、本発明の実施例を図面に基
づいてより詳細に説明する。Embodiments of the present invention will be described below in detail with reference to the drawings.

【００１６】図１は、本発明の水素・酸素発生装置の全
体の概略図である。FIG. 1 is a schematic view of the entire hydrogen / oxygen generator of the present invention.

【００１７】図１において、１は全体で水素・酸素発生
器を示しており、水素・酸素発生器１は、水電解セル２
を備え、この水電解セル２は純水容器３内に収納されて
おり、純水容器３内には純水が充填されており、水電解
セル２の陽極側に通じる開口24から水電解セル２内に純
水が供給されて、純水容器３の外部に設けられた電源
（図示せず）から、陽極側と陰極側に電圧が印可され
て、電気分解が行われ、陽極側から酸素ガスが、陰極側
から水素ガスがそれぞれ発生するようになっている。な
お、水電解セル２の内部構造は図示を省略するが、これ
は図２に示したように、固体高分子電解質膜等の電解質
膜を隔膜として用いて、陽極側と陰極側とに分離して、
純水を陽極側に供給しながら純水を電気分解して、陽極
側から酸素ガスを、陰極側から水素ガスをそれぞれ発生
するように構成されたものである。このような水電解セ
ルの構造として、本発明者等が既に出願した特願平7-24
737 号「水素・酸素ガス発生装置」に開示したものが使
用可能である。In FIG. 1, reference numeral 1 denotes a hydrogen / oxygen generator as a whole, and the hydrogen / oxygen generator 1 is a water electrolysis cell 2
This water electrolysis cell 2 is housed in a pure water container 3, and the pure water container 3 is filled with pure water. The water electrolysis cell 2 is opened through an opening 24 communicating with the anode side of the water electrolysis cell 2. 2 is supplied with pure water, a voltage is applied to the anode side and the cathode side from a power source (not shown) provided outside the pure water container 3, electrolysis is performed, and oxygen is supplied from the anode side. Hydrogen gas is generated from the cathode side. Although the internal structure of the water electrolysis cell 2 is not shown, as shown in FIG. 2, it is separated into an anode side and a cathode side by using an electrolyte membrane such as a solid polymer electrolyte membrane as a diaphragm. hand,
The pure water is electrolyzed while supplying the pure water to the anode side to generate oxygen gas from the anode side and hydrogen gas from the cathode side. As a structure of such a water electrolysis cell, Japanese Patent Application No. 7-24 filed by the present inventors has already applied.
The one disclosed in No. 737 “Hydrogen / oxygen gas generator” can be used.

【００１８】そして、水電解セル２の陽極側から発生し
た酸素ガスは、純水容器３の上方に形成された酸素ガス
気液分離室４に溜まり、図示しない圧力制御装置の制御
によって、酸素ガス気液分離室４から所定の圧力になっ
た際に、酸素ガス取り出しライン５を介して、貯蔵タン
クなどのユースポイントに供給されるようになってい
る。Then, the oxygen gas generated from the anode side of the water electrolysis cell 2 collects in the oxygen gas gas-liquid separation chamber 4 formed above the pure water container 3, and the oxygen gas is controlled by a pressure control device (not shown). When a predetermined pressure is reached from the gas-liquid separation chamber 4, it is supplied to a use point such as a storage tank via an oxygen gas extraction line 5.

【００１９】一方、水電解セル２の陰極側から発生した
水素ガスは、水素取り出し管６を介して、純水容器３の
外部に配設された水素ガス気液分離装置７に導入されて
気液分離された後、図示しない圧力制御装置の制御によ
って、水素ガス気液分離装置７から所定の圧力になった
際に、水素ガス取り出しライン８を介して、貯蔵タンク
などのユースポイントに供給されるようになっている。On the other hand, the hydrogen gas generated from the cathode side of the water electrolysis cell 2 is introduced into the hydrogen gas gas-liquid separation device 7 arranged outside the pure water container 3 via the hydrogen take-out pipe 6 and vaporized. After the liquid separation, under the control of a pressure control device (not shown), when the hydrogen gas vapor-liquid separation device 7 reaches a predetermined pressure, it is supplied to a use point such as a storage tank via a hydrogen gas extraction line 8. It has become so.

【００２０】さらに、純水容器３には、酸素ガス気液分
離室４の液面位置を検出するための純水容器液面検知装
置９が設けられており、この純水容器液面検知装置９
は、酸素ガス気液分離室４の側部に配設された水面計10
と水面センサ11と水面検出制御装置12とから構成されて
いる。Further, the deionized water container 3 is provided with a deionized water container liquid level detection device 9 for detecting the liquid level position of the oxygen gas gas-liquid separation chamber 4. This deionized water container liquid level detection device is provided. 9
Is a water level gauge 10 arranged on the side of the oxygen gas gas-liquid separation chamber 4.
It is composed of a water surface sensor 11 and a water surface detection control device 12.

【００２１】さらに、電気分解反応が進むにしたがっ
て、純水容器内の純水が消費されていくので、補給水タ
ンク14は、純水容器３内に純水を補給するために、純水
容器３よりも高い水平位置に配設され、且つ補給水経路
13を介して純水容器３の酸素ガス気液分離室４に接続さ
れている。なお、補給水経路13には補給水経路開閉弁Ｄ
が設けられるとともに、補給水タンク14の上部には、ガ
ス抜き経路15が設けられ、ガス抜き弁Ａが配設されてい
る。また、補給水タンク14には、補給水タンク14の液面
位置を検出するための補給水タンク液面検知装置16が設
けられており、この補給水タンク液面検知装置16は、補
給水タンク14の側部に配設された水面計17と水面センサ
18と水面検出制御装置19とから構成されている。Further, since the pure water in the pure water container is consumed as the electrolysis reaction progresses, the make-up water tank 14 uses the pure water container 14 to replenish the pure water container 3 with pure water. It is installed in a horizontal position higher than 3 and the makeup water path
It is connected to the oxygen gas gas-liquid separation chamber 4 of the pure water container 3 via 13. In addition, the makeup water passage opening / closing valve D is provided in the makeup water passage 13.
Is provided, a gas vent path 15 is provided above the makeup water tank 14, and a gas vent valve A is provided. Further, the makeup water tank 14 is provided with a makeup water tank liquid level detection device 16 for detecting the liquid level position of the makeup water tank 14, and this makeup water tank liquid level detection device 16 is a makeup water tank. Water level gauge 17 and water level sensor installed on the side of 14
18 and a water surface detection control device 19.

【００２２】一方、補給水タンク14上部と純水容器３の
酸素ガス気液分離室４の上部は、連通経路22を介して連
通されるとともに、連通経路22には連通経路開閉弁Ｂが
設けられている。On the other hand, the upper portion of the makeup water tank 14 and the upper portion of the oxygen gas gas-liquid separation chamber 4 of the pure water container 3 are communicated with each other through the communication passage 22, and the communication passage 22 is provided with a communication passage opening / closing valve B. Has been.

【００２３】また、純水タンク21は、補給水タンク14に
純水を供給するために、補給水タンクよりも高い水平位
置に配設され、且つ純水供給経路20を介して補給水タン
ク上部に接続される。また、前記純水供給経路20には純
水供給経路開閉弁Ｃが設けられている。The pure water tank 21 is disposed at a horizontal position higher than that of the makeup water tank in order to supply the makeup water tank 14 with pure water, and the upper portion of the makeup water tank via the pure water supply path 20. Connected to. The pure water supply passage 20 is provided with a pure water supply passage open / close valve C.

【００２４】このように構成される本発明の水素・酸素
発生装置において、純水を純水容器３内に供給する場合
の作動について、以下に説明する。In the hydrogen / oxygen generator of the present invention having the above-described structure, the operation of supplying pure water into the pure water container 3 will be described below.

【００２５】水電解セル２の電気分解反応が進むにした
がって、純水容器３内の純水が消費されていくので、純
水容器３の上方に形成された酸素ガス気液分離室４の液
面位置は低くなる。この液面位置が、純水容器液面検知
装置９の水面計10と水面センサ11によって所定のレベル
位置を下回ったと検出された場合に、水面検出制御装置
12から制御信号が出される。この制御信号によって、補
給水経路13の補給水経路開閉弁Ｄ及び連通経路22の連通
経路開閉弁Ｂを閉止した状態で、純水供給経路20の純水
供給経路開閉弁Ｃ及びガス抜き経路15のガス抜き弁Ａを
開放する制御が行われる。この結果、純水タンク21が補
給水タンク14より高水平位置に配置されているので、純
水タンク21と補給水タンク14との水位差によって、補給
水は純水タンク21より補給水タンク14に供給される。Since the pure water in the pure water container 3 is consumed as the electrolysis reaction of the water electrolysis cell 2 progresses, the liquid in the oxygen gas gas-liquid separation chamber 4 formed above the pure water container 3 The surface position becomes low. When it is detected by the water level gauge 10 and the water level sensor 11 of the pure water container liquid level detection device 9 that this liquid level position is below a predetermined level position, the water level detection control device
Control signal is issued from 12. With this control signal, the pure water supply passage opening / closing valve C and the degassing passage 15 of the pure water supply passage 20 are closed with the makeup water passage opening / closing valve D of the makeup water passage 13 and the communication passage opening / closing valve B of the communication passage 22 closed. The control for opening the gas vent valve A is performed. As a result, since the pure water tank 21 is arranged at a higher horizontal position than the makeup water tank 14, the makeup water is supplied from the makeup water tank 14 to the makeup water tank 14 due to the water level difference between the makeup water tank 21 and the makeup water tank 14. Is supplied to.

【００２６】そして、補給水タンク液面検知装置16の水
面計17と水面センサ18によって検知された補給水タンク
の液面位置が、予め設定されたレベルよりも高くなる
と、水面検出制御装置19から制御信号が発信される。こ
の制御信号によって、純水供給経路20の純水供給経路開
閉弁Ｃ及びガス抜き経路15のガス抜き弁Ａを閉止すると
ともに、連通経路22の連通経路開閉弁Ｂを開放する弁の
制御が行われる。その結果、補給水タンク14内と純水容
器３内の圧力が同圧力になる。なお、この場合、補給水
タンクの液面位置の予め設定されたレベルを、ガス抜き
弁Ａから補給水がリークしてくるような満水レベル位置
に設定しておけば、補給水タンク14内に気体（酸素ガ
ス）が存在しないので、純水容器３内の圧力が低下する
ことがなく、酸素ガス圧を一定の圧力で酸素ガス取り出
しライン５を介して、貯蔵タンクなどのユースポイント
に供給される。When the liquid level position of the makeup water tank detected by the water level gauge 17 and the water level sensor 18 of the makeup water tank liquid level detection device 16 becomes higher than a preset level, the water level detection control device 19 A control signal is emitted. By this control signal, the deionized water supply path opening / closing valve C of the deionized water supply path 20 and the degassing valve A of the degassing path 15 are closed, and the valve for opening the communicating path opening / closing valve B of the communicating path 22 is controlled. Be seen. As a result, the pressures in the makeup water tank 14 and the pure water container 3 become the same. In this case, if the preset level of the liquid surface position of the makeup water tank is set to a full water level position where the makeup water leaks from the gas vent valve A, the inside of the makeup water tank 14 will be Since there is no gas (oxygen gas), the pressure in the pure water container 3 does not drop, and the oxygen gas pressure is supplied at a constant pressure to the use point such as a storage tank via the oxygen gas extraction line 5. It

【００２７】次に、図示しないが補給水タンク14内と純
水容器３内に設けられた圧力センサーの測定の結果、補
給水タンク14内と純水容器３内の圧力が同圧力となった
後に、補給水経路13の補給水経路開閉弁Ｄを開放する
と、補給水タンク14は純水容器３より高水平位置に配置
されているので、補給水タンク14と純水容器３との水位
差によって、補給水は補給水タンク14から純水容器３に
供給される。Next, as a result of measurement by pressure sensors (not shown) provided in the makeup water tank 14 and the pure water container 3, the pressures in the makeup water tank 14 and the pure water container 3 became equal. After that, when the make-up water passage opening / closing valve D of the make-up water passage 13 is opened, the make-up water tank 14 is arranged at a higher horizontal position than the pure water container 3, so that the water level difference between the make-up water tank 14 and the pure water container 3 is increased. Thus, the makeup water is supplied from the makeup water tank 14 to the pure water container 3.

【００２８】そして、酸素ガス気液分離室４の液面位置
が、純水容器液面検知装置９の水面計10と水面センサ11
によって所定のレベル位置を上回ったと検出された場合
に、水面検出制御装置12から制御信号が出されて、連通
経路22の連通経路開閉弁Ｂ及び補給水経路13の補給水経
路開閉弁Ｄが閉止されて純水容器３内への補給水の供給
が完了し、次の補給水供給サイクルが順次繰り返し行わ
れるようになっている。The liquid level of the oxygen gas gas-liquid separation chamber 4 is determined by the water level gauge 10 and the water level sensor 11 of the pure water container liquid level detection device 9.
When it is detected by the water level detection control device 12 that a predetermined level position is exceeded, a control signal is output from the water surface detection control device 12 to close the communication path opening / closing valve B of the communication path 22 and the makeup water path opening / closing valve D of the makeup water path 13. Then, the supply of makeup water into the pure water container 3 is completed, and the next makeup water supply cycle is sequentially repeated.

【００２９】なお、上述した実施例では、純水容器３の
上部に酸素ガス気液分離室４のみを設けてあるが、図示
しないが、その代わりに、純水容器３内を隔壁によって
二分して、酸素ガス気液分離室と水素ガス気液分離室を
形成して、いずれか一方又は両方の気液分離室に補給水
タンクから純水を補給するように構成することも可能で
ある。In the above-described embodiment, only the oxygen gas gas-liquid separation chamber 4 is provided above the pure water container 3, but not shown, but instead, the inside of the pure water container 3 is divided by a partition wall. It is also possible to form an oxygen gas gas-liquid separation chamber and a hydrogen gas gas-liquid separation chamber, and to supply pure water to either or both gas-liquid separation chambers from the makeup water tank.

【００３０】[0030]

【発明の効果】本発明の水素・酸素発生装置によれば、
純水容器液面位置が、予め設定されたレベルより低い場
合に、補給水経路及び連通経路を閉止した状態で、純水
供給経路及びガス抜き経路を開放して、純水タンクと補
給水タンクとの水位差によって、純水タンクより補給水
タンクに補給水が供給され、補給水タンク液面位置が予
め設定されたレベルよりも高い場合に、純水供給経路及
びガス抜き経路を閉止するとともに、連通経路を開放し
て、補給水タンク内と水素・酸素発生器の純水容器内を
同圧力とし、補給水タンク内と水素・酸素発生器の純水
容器内を同圧力となった後に、補給水経路を開放して、
補給水タンクと水素・酸素発生器の純水容器との水位差
によって、補給水を補給水タンクから純水容器に供給す
るように構成したので、高圧ポンプなどの動力源を用い
ることなく、純水容器内の高圧を維持したまま、純水容
器内の純水のガス発生に消費された純水を、補充水とし
て容易に補充可能であり、高圧ポンプなどの構成部品の
潤滑オイル等による不純物が混入するおそれがなく、高
純度で且つ高圧の酸素ガス、水素ガスを提供できる。According to the hydrogen / oxygen generator of the present invention,
When the liquid surface position of the pure water container is lower than the preset level, the pure water supply path and the degassing path are opened with the makeup water path and the communication path closed, and the pure water tank and the makeup water tank When the makeup water is supplied from the deionized water tank to the makeup water tank due to the water level difference between and, and the liquid level position of the makeup water tank is higher than the preset level, the deionized water supply path and the degassing path are closed. After opening the communication path, the pressure in the makeup water tank and the deionized water container of the hydrogen / oxygen generator are set to the same pressure, and the pressure in the makeup water tank and the deionized water container of the hydrogen / oxygen generator are set to the same pressure. , Open the make-up water channel,
Since the makeup water is supplied from the makeup water tank to the pure water container by the water level difference between the makeup water tank and the pure water container of the hydrogen / oxygen generator, it is possible to use pure water without using a power source such as a high-pressure pump. Pure water consumed for generating pure water gas in the pure water container can be easily replenished as supplementary water while maintaining the high pressure in the water container. It is possible to provide high-purity and high-pressure oxygen gas and hydrogen gas without the risk of being mixed in.

【図面の簡単な説明】[Brief description of drawings]

【図１】図１は、本発明の水素・酸素発生装置の全体の
概略図である。FIG. 1 is a schematic view of the entire hydrogen / oxygen generator of the present invention.

【図２】図２は、水電解セルの構成を示す概略図であ
る。FIG. 2 is a schematic diagram showing a configuration of a water electrolysis cell.

【符号の説明】[Explanation of symbols]

１・・・ 水素・酸素発生器 ２・・・ 水電解セル ３・・・ 純水容器 ４・・・ 酸素ガス気液分離室 ５・・・ 酸素ガス取り出しライン ６・・・ 水素取り出し管 ７・・・ 水素ガス気液分離装置 ８・・・ 水素ガス取り出しライン ９・・・ 純水容器液面検知装置 １０・・・ 水面計 １１・・・ 水面センサ １２・・・ 水面検出制御装置 １３・・・ 補給水経路 １４・・・ 補給水タンク １５・・・ ガス抜き経路 １６・・・ 補給水タンク液面検知装置 １７・・・ 水面計 １８・・・ 水面センサ １９・・・ 水面検出制御装置 ２０・・・ 純水供給経路 ２１・・・ 純水タンク ２２・・・ 連通経路 ２４・・・ 開口 Ａ・・・ ガス抜き弁 Ｂ・・・ 連通経路開閉弁 Ｃ・・・ 純水供給経路開閉弁 Ｄ・・・ 補給水経路開閉弁 1 ... Hydrogen / oxygen generator 2 ... Water electrolysis cell 3 ... Pure water container 4 ... Oxygen gas gas-liquid separation chamber 5 ... Oxygen gas extraction line 6 ... Hydrogen extraction tube 7 ...・ ・ Hydrogen gas gas-liquid separator 8 ・ ・ ・ Hydrogen gas take-out line 9 ・ ・ ・ Pure water container liquid level detector 10 ・ ・ ・ Water level gauge 11 ・ ・ ・ Water level sensor 12 ・ ・ ・ Water level detection controller 13 ・・ Replenishment water route 14 ・ ・ ・ Replenishment water tank 15 ・ ・ ・ Gas release route 16 ・ ・ ・ Replenishment water tank liquid level detection device 17 ・ ・ ・ Water level gauge 18 ・ ・ ・ Water level sensor 19 ・ ・ ・ Water level detection control device 20・ ・ ・ Pure water supply path 21 ・ ・ ・ Pure water tank 22 ・ ・ ・ Communication path 24 ・ ・ ・ Opening A ・ ・ ・ Gas vent valve B ・ ・ ・ Communication path opening / closing valve C ・ ・ ・ Pure water supply path opening / closing valve D ... Make-up water passage opening / closing valve

───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐々木 隆 兵庫県三木市志染町東自由が丘３丁目310 (72)発明者 平井 清司 兵庫県加古川市別府町新野辺475−20 (72)発明者 長尾 衛 大阪府大阪市東淀川区井高野２丁目７番18 −102号 (72)発明者 原田 宙幸 東京都練馬区西大泉２−25−43 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Takashi Sasaki, Takashi Higashi Jiyugaoka, Shizen Town, Miki City, Hyogo Prefecture 310 (72) Inventor, Kiyoji Hirai, Shinnobe, Beppu Town, Kakogawa City, Hyogo Prefecture, 475-20 (72) Mamoru Nagao Osaka 2-7-18-102 Itakano, Higashiyodogawa-ku, Osaka-shi, Japan (72) Inventor Hiroyuki Harada 2-25-43 Nishi-oizumi, Nerima-ku, Tokyo

Claims (4)

【特許請求の範囲】[Claims] 【請求項１】 固体高分子電解質膜等の電解質膜を隔膜
として用いて、陽極側と陰極側とに分離して、純水を陽
極側に供給しながら純水を電気分解して、陽極側から酸
素ガスを、陰極側から水素ガスをそれぞれ発生するよう
に構成され、且つ純水容器内に収容された水電解セルを
備えた水素・酸素発生器と、 水素・酸素発生器の純水容器内に純水を補給するため
に、水素・酸素発生器の純水容器よりも高水平位置に配
設され、且つ補給水経路を介して水素・酸素発生器の純
水容器に接続された補給水タンクと、 補給水タンク上方に配設されたガス抜き経路と、 補給水タンクに純水を供給するために、補給水タンクよ
りも高水平位置に配設され、且つ純水供給経路を介して
補給水タンクに接続された純水タンクと、 水素・酸素発生器の純水容器上部と補給水タンクの上部
を連通する連通経路とから構成され、 純水タンク、補給水タンク、及び純水容器の水位差によ
って、純水タンクから補給水タンクを介して、水素・酸
素発生器の純水容器内に補給するように構成したことを
特徴とする水素・酸素発生装置。1. An electrolyte membrane such as a solid polymer electrolyte membrane is used as a diaphragm to separate it into an anode side and a cathode side, and the pure water is electrolyzed while supplying the pure water to the anode side. Hydrogen / oxygen generator equipped with a water electrolysis cell that is configured to generate oxygen gas from the cathode and hydrogen gas from the cathode side, and a pure water container of the hydrogen / oxygen generator. In order to replenish the inside with pure water, the replenishment is arranged at a higher horizontal position than the pure water container of the hydrogen / oxygen generator and is connected to the pure water container of the hydrogen / oxygen generator through the replenishing water path. A water tank, a degassing path arranged above the makeup water tank, and a pure water supply path which is arranged at a higher horizontal position than the makeup water tank for supplying pure water to the makeup water tank. Pure water tank connected to the makeup water tank and the pure water volume of the hydrogen / oxygen generator. A hydrogen / oxygen generator from the pure water tank through the makeup water tank, depending on the water level difference between the pure water tank, the makeup water tank, and the pure water container. A hydrogen / oxygen generator characterized in that it is configured to be replenished in the pure water container. 【請求項２】 水素・酸素発生器の純水容器には、純水
容器の液面位置を検出するための純水容器液面検知装置
が設けられており、 純水容器液面検知装置によって検知された純水容器液面
位置が、予め設定されたレベルより低い場合に、補給水
経路及び連通経路を閉止した状態で、純水供給経路及び
ガス抜き経路を開放して、純水タンクと補給水タンクと
の水位差によって、純水タンクより補給水タンクに補給
水を供給するように構成され、 補給水タンクには、補給水タンクの液面位置を検出する
ための補給水タンク液面検知装置が設けられており、 補給水タンク液面検知装置によって検知された補給水タ
ンク液面位置が予め設定されたレベルよりも高い場合
に、純水供給経路及びガス抜き経路を閉止するととも
に、連通経路を開放して、補給水タンク内と水素・酸素
発生器の純水容器内を同圧力とするように構成され、 補給水タンク内と水素・酸素発生器の純水容器内が同圧
力となった後に、補給水経路を開放して、補給水タンク
と水素・酸素発生器の純水容器との水位差によって、補
給水を補給水タンクから純水容器に供給するように構成
されていることを特徴とする請求項１に記載の水素・酸
素発生装置。2. The pure water container of the hydrogen / oxygen generator is provided with a pure water container liquid level detection device for detecting the liquid surface position of the pure water container. When the detected liquid level of the pure water container is lower than the preset level, open the pure water supply route and the degassing route with the makeup water route and the communication route closed, and connect with the pure water tank. The make-up water is configured to be supplied from the pure water tank to the make-up water tank by the water level difference from the make-up water tank. The make-up water tank has a make-up water tank liquid level for detecting the position of the make-up water tank liquid level. A detector is provided and closes the pure water supply path and the degassing path when the makeup water tank liquid level position detected by the makeup water tank liquid level detection device is higher than a preset level, and Open the communication path to supplement The water supply tank and the deionized water container of the hydrogen / oxygen generator are configured to have the same pressure, and the makeup water path is set after the replenishment water tank and the deionized water container of the hydrogen / oxygen generator have the same pressure. Is opened, and the makeup water is supplied from the makeup water tank to the pure water container by a water level difference between the makeup water tank and the pure water container of the hydrogen / oxygen generator. 1. The hydrogen / oxygen generator according to 1. 【請求項３】 補給水タンク液面位置の予め設定された
レベルが、満水レベルとなるように設定されていること
を特徴とする請求項２に記載の水素・酸素発生装置。3. The hydrogen / oxygen generator according to claim 2, wherein a preset level of the liquid surface position of the makeup water tank is set to be a full water level. 【請求項４】 補給水経路、ガス抜き経路、純水供給経
路及び連通経路の開閉を、それぞれの経路に設けた開閉
弁によって行うように構成されていることを特徴とする
請求項２又は３に記載の水素・酸素発生装置。4. A makeup water passage, a gas vent passage, a pure water supply passage, and a communication passage are configured to be opened / closed by opening / closing valves provided in the respective passages. The hydrogen / oxygen generator described in.
JP23399695A 1995-09-12 1995-09-12 Hydrogen / oxygen generator Expired - Lifetime JP3487687B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23399695A JP3487687B2 (en) 1995-09-12 1995-09-12 Hydrogen / oxygen generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23399695A JP3487687B2 (en) 1995-09-12 1995-09-12 Hydrogen / oxygen generator

Publications (2)

Publication Number Publication Date
JPH0978278A true JPH0978278A (en) 1997-03-25
JP3487687B2 JP3487687B2 (en) 2004-01-19

Family

ID=16963923

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23399695A Expired - Lifetime JP3487687B2 (en) 1995-09-12 1995-09-12 Hydrogen / oxygen generator

Country Status (1)

Country Link
JP (1) JP3487687B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8057646B2 (en) 2004-12-07 2011-11-15 Hydrogenics Corporation Electrolyser and components therefor
JP2022080108A (en) * 2020-11-17 2022-05-27 株式会社神鋼環境ソリューション Hydrogen/oxygen generator, and gas liquid separation tank

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8057646B2 (en) 2004-12-07 2011-11-15 Hydrogenics Corporation Electrolyser and components therefor
JP2022080108A (en) * 2020-11-17 2022-05-27 株式会社神鋼環境ソリューション Hydrogen/oxygen generator, and gas liquid separation tank

Also Published As

Publication number Publication date
JP3487687B2 (en) 2004-01-19

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