JPS63100190A - Electrolytic device for generating gas - Google Patents
Electrolytic device for generating gasInfo
- Publication number
- JPS63100190A JPS63100190A JP61246578A JP24657886A JPS63100190A JP S63100190 A JPS63100190 A JP S63100190A JP 61246578 A JP61246578 A JP 61246578A JP 24657886 A JP24657886 A JP 24657886A JP S63100190 A JPS63100190 A JP S63100190A
- Authority
- JP
- Japan
- Prior art keywords
- anode
- anolyte
- gas
- electrolytic device
- collector electrode
- 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.)
- Pending
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
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は酸素、オゾン、塩素等のガスを陽極で発生さ
せるためのオンサイト型のガス発生用電解装置に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an on-site type gas generation electrolyzer for generating gases such as oxygen, ozone, chlorine, etc. at an anode.
(従来の技術)
水電解法で酸素またはオゾン含有酸素を、また塩酸電解
法で塩素を発生させる方法は公知技術に属する。従来技
術におけるガス発生用電解装置は一般に行なわれるシス
テムを踏襲しているものが多く、例えば、水電解による
オゾン含有酸素発生の場合には第4図のようにヨーロッ
パ公開特許第82200493号明細書に開示されてい
るが、電解液を溜め、別個に設けられた電解槽にポンプ
で強制的に電解液を送給するなど、複雑な構成となって
おり、コンパクト、省人力、高安全性で、かつ安価な装
置が望まれている。このような要求に合致したガス発生
用電解装置は従来の電解槽構造では達成困難であり、こ
れまでに知られていない。(Prior Art) A method of generating oxygen or ozone-containing oxygen by water electrolysis and a method of generating chlorine by hydrochloric acid electrolysis belong to known techniques. Many conventional electrolyzers for gas generation follow commonly used systems. For example, in the case of ozone-containing oxygen generation by water electrolysis, as shown in Figure 4, European Patent Publication No. 82200493 describes Although disclosed, it has a complicated configuration, such as storing electrolyte and forcibly feeding the electrolyte to a separately installed electrolytic tank using a pump.It is compact, labor-saving, and highly safe. Moreover, an inexpensive device is desired. An electrolytic device for gas generation that meets such requirements is difficult to achieve with conventional electrolytic cell structures, and has not been known to date.
(発明が解決しようとする問題点)
オンサイト型のガス発生装置が、従来からのガスボンベ
による酸素・塩素等の輸送、保管上の問題点(遠隔地ま
での輸送上の、また高圧ガス取締法、劇毒物取締法によ
る保管上の問題点)に代えて有効な手段となるためには
、コンパクトであること、運転・保守が容易で人力を必
要とせず、安全でかつ経済的なものとしなければならな
い。このためには前記した従来技術のごときポンプを利
用した強制循環機構を有するものでは、構成が複雑とな
るため必ずしも好適ではなく、一方自然循環型のもので
は、作動中に部分的に液切れを起す危険性があるため電
流密度を高くすることができず、どうしても大型の装置
となり、かつ安全上の問題がある。発明者らはこれらの
問題点を解決すべく、従来の工業電解システムとは全く
異なる電解槽構造を考案した。(Problems to be Solved by the Invention) On-site gas generators have problems with the transportation and storage of oxygen, chlorine, etc. using conventional gas cylinders (such as transportation to remote locations, and High Pressure Gas Control Law). In order to become an effective means to replace the storage problems under the Poisonous Substances Control Law), it must be compact, easy to operate and maintain, do not require human labor, be safe, and be economical. Must be. For this purpose, a device with a forced circulation mechanism using a pump such as the above-mentioned conventional technology is not necessarily suitable because the structure is complicated, while a natural circulation type device prevents liquid from partially running out during operation. The current density cannot be increased because of the risk of causing a nuisance, which inevitably results in a large device and poses a safety problem. In order to solve these problems, the inventors devised an electrolytic cell structure that is completely different from conventional industrial electrolysis systems.
(問題点を解決するための手段)
コンパクトな即ち高電流密度電解槽を作製するためには
、電極面における電流密度分布が均一であることが好ま
しい。また、電極反応面に陽極液の供給が常に一定に保
たれ、枯渇する部分を作らないようにすることが必要で
ある。もし、枯渇する部分が発生すると、電気抵抗が上
昇し、発熱によって電極を破損し、事故の原因となる。(Means for Solving the Problems) In order to produce a compact, ie, high current density electrolytic cell, it is preferable that the current density distribution on the electrode surface be uniform. Furthermore, it is necessary to always maintain a constant supply of anolyte to the electrode reaction surface so as not to create a depleted portion. If a depleted portion occurs, the electrical resistance will increase and the electrodes will be damaged due to heat generation, causing an accident.
高電流密度電解槽で好ましい槽の構成は、固体高分子電
解質膜とこれに給電するための接触点を多くもつ多孔質
集電極を一組として、両側より1陽・陰極で締付けて組
立てる。A preferred configuration of a high current density electrolytic cell is to assemble a solid polymer electrolyte membrane and a porous collector electrode having many contact points for supplying power to the membrane as a set, which are tightened from both sides with one anode and one cathode.
本発明は発生ガスの円滑な取り出しと、電極反応面への
陽極液の供給が中断することなく、常に陽極液に接触で
きるように配慮したものであり、上部主陽極とこれに接
する上部多孔質集電極、固体高分子電解質膜、下部多孔
質集電極と、下部主陰極とが積層して形成されたガス発
生用電解装置において、該上部電極側に陽極液溜容器を
直結して陽極を陽極液面下に保つガス発生用電解装置、
上部主陽極にガスリフト管を備え、離れた位置に複数個
の給液用孔を設けた陽極液循環機構を有するガス発生用
電解装置、及び電解室側に溝を加工し、溝深さを中心部
に向けて円錐状の傾斜をもたせた主陽極による発生ガス
集合手段とを備えたガス発生用電解装置を要旨とするも
のである。The present invention is designed to ensure smooth extraction of generated gas and constant contact with the anolyte without interruption in the supply of anolyte to the electrode reaction surface. In an electrolytic device for gas generation formed by laminating a collector electrode, a solid polymer electrolyte membrane, a lower porous collector electrode, and a lower main cathode, an anode liquid reservoir is directly connected to the upper electrode side, and the anode is connected to the anode. Electrolyzer for gas generation kept below the liquid level,
An electrolytic device for gas generation that has a gas lift pipe on the upper main anode and an anolyte circulation mechanism with multiple liquid supply holes at separate locations, and a groove is machined on the electrolytic chamber side, with the groove depth centered around the The gist of the present invention is an electrolytic device for gas generation, which is equipped with a generated gas collecting means using a main anode having a conical slope toward the bottom.
(作用効果)
このように本発明におけるガス発生用電解装置は、上部
主陽極と、これに接する上部多孔質集電極、固体高分子
電解質膜、下部多孔質集電極と、下部主陰極とが積層し
て形成され、しかも該上部電極側に電解液溜容器を直結
して陽極を電解液面下に位置させたから、該電極の陽極
側には陽極液が常に存在して電解は中断することなく続
行でき、しかも陽極液中に設けたガスリフト管等による
陽極液循環機構は、陽極液枯渇による電極の損傷を防止
できるとともに、発生ガスの上昇が駆動源となって、陽
極液循環がよく行われ、電極への陽極液の供給は確実と
なり、従来のように陽極液を強制的に送るポンプは不要
で、故障がなく装置はコンパクトにまとまり、高電流密
度、たとえば60A/drn” 〜150A/di
の運転が可能となる。因みに従来の自然循環タイプの
ものでは30〜60A/drrl’が限度であった。(Operation and Effect) As described above, the electrolytic device for gas generation according to the present invention has an upper main anode, an upper porous collector electrode in contact with the upper main anode, a solid polymer electrolyte membrane, a lower porous collector electrode, and a lower main cathode that are laminated. Moreover, since the electrolyte reservoir is directly connected to the upper electrode side and the anode is positioned below the electrolyte surface, the anolyte is always present on the anode side of the electrode, and the electrolysis is not interrupted. In addition, the anolyte circulation mechanism using a gas lift tube installed in the anolyte prevents damage to the electrode due to depletion of the anolyte, and the anolyte is well circulated because the rising gas generated serves as a driving source. , the anolyte is reliably supplied to the electrode, there is no need for a pump to forcefully feed the anolyte as in the past, there is no failure, the device is compact, and it has a high current density, e.g. 60A/drn” to 150A/di.
It becomes possible to drive. Incidentally, in the conventional natural circulation type, the limit was 30 to 60 A/drrl'.
更に主陽極には電解室側に傾斜溝による発生ガス集合手
段を設けたから、ガスは傾斜に沿って上昇集合し、電極
面に滞留することがなくなり電解効率の向上に役立つ。Furthermore, since the main anode is provided with a generated gas collection means by an inclined groove on the electrolytic chamber side, the gas collects upward along the inclination and does not stay on the electrode surface, which helps to improve the electrolytic efficiency.
上記のような構造は、従来の電解方式に見られる電解液
貯槽、送液機、大型の電解槽、気液分離器といったシス
テムを無くし、極めて簡略化した装置を実用化でき、こ
の結果、コンパクトになり、かつ運転・保守装置が簡略
化される効果がある。The structure described above eliminates systems such as electrolyte storage tank, liquid feeder, large electrolytic tank, and gas-liquid separator that are found in conventional electrolysis methods, making it possible to put into practical use an extremely simple device.As a result, it is compact and compact. This has the effect of simplifying the operation and maintenance equipment.
(実用例)
以下本発明の一実施例として、水の電解によるオゾン含
有酸素発生用電解装置を説明する。第1図、第2図にお
いて、ガス発生用電解装置1は、上部主陽極2とこれに
接する上部多孔質集電極3、固体高分子電解質膜4、下
部多孔質集電極5と下部主陰極6とが積層し、Oリング
22を介し絶縁スリーブで被覆したボルト7で緊締され
ている。(Practical Example) As an example of the present invention, an electrolytic device for generating ozone-containing oxygen by electrolyzing water will be described below. 1 and 2, an electrolytic device 1 for gas generation includes an upper main anode 2, an upper porous collector electrode 3 in contact therewith, a solid polymer electrolyte membrane 4, a lower porous collector electrode 5, and a lower main cathode 6. are laminated and tightened with a bolt 7 covered with an insulating sleeve via an O-ring 22.
上部主陽極2は、通常陽極側の酸化性ガスに耐える金属
としてチタン、タンタル、ニオブ等が使用される。上部
多孔質集電極3の材料には、上記金属の多孔体を機械加
工、電解加工、溶出法あるいは焼結法によって作製した
ものをそのまま、もしくはさらにその表面に白金族金属
または酸化物、二酸化鉛等の触媒金属もしくは酸化物を
被覆したものが使用される。For the upper main anode 2, titanium, tantalum, niobium, or the like is normally used as a metal that can withstand oxidizing gas on the anode side. The material of the upper porous collector electrode 3 may be a porous body of the above-mentioned metal produced by machining, electrolytic processing, elution method, or sintering method, or a platinum group metal, oxide, or lead dioxide may be added to the surface. Those coated with catalytic metals or oxides such as catalytic metals are used.
下部主陰極6はチタン、ステンレス鋼(陽極液が塩酸以
外の場合)または炭素が使用される。下部多孔質集電極
5の材料は、発生水素および同伴水または同伴電解液に
耐蝕性のある多孔性炭素板が多く使用され、この多孔性
炭素板は主に焼結法で作製される。The lower main cathode 6 is made of titanium, stainless steel (if the anolyte is other than hydrochloric acid), or carbon. As the material for the lower porous collector electrode 5, a porous carbon plate that is resistant to corrosion by generated hydrogen and entrained water or entrained electrolyte is often used, and this porous carbon plate is mainly produced by a sintering method.
陰陽極室を分離する隔膜には、固体高分子電解質膜を使
用する。但し実用的には、陽極で発生するオゾン含有酸
素に十分の耐性をもつフッ素系イオン交換膜が使用され
る。この型の膜の代表的な商品にはデュポン社のNAF
ION膜がある。このイオン交換膜は原膜のまま陰陽電
極を押付けて使用するか、またはあらかじめ触媒電極層
を膜面に接合させた膜−電極接合体を作製し、これに両
面から多孔質集電極を押付けて使用する。A solid polymer electrolyte membrane is used as the diaphragm that separates the cathode and anode chambers. However, in practice, a fluorine-based ion exchange membrane is used which has sufficient resistance to ozone-containing oxygen generated at the anode. Representative products of this type of membrane include DuPont's NAF
There is an ION membrane. This ion-exchange membrane can be used as a raw membrane by pressing negative and positive electrodes, or by preparing a membrane-electrode assembly in which a catalyst electrode layer is bonded to the membrane surface in advance, and pressing porous collector electrodes onto this from both sides. use.
上部主陽極2は中心に陽極液出口孔8と、周辺に複数個
の陽極液取入孔9が穿設されており、例えば上部取出口
10と側方に陽極液人口11のある陽極液溜容器、例え
ばガラスペルジャー12で覆われ、植込ボルト13で上
部主陽極2に固着されており、陽極液は水位14を保ち
、これによって上部多孔質集電極3が常に液面下にあっ
て上部多孔質集電極3への陽極液の供給は円滑に行われ
、この多孔質集電極3は電力を供給し、発生オゾン含有
酸素を拡散する。しかも、内部には基部15が前記陽極
液出口孔8に連絡し、上端16がガラスペルジャー12
内に開口するガスリフト管17が設けられており、これ
らの陽極液取入孔9、上部多孔質集電極3、電解液出口
孔8及びガスリフト管17によって陽極液循環機構18
が形成されていて、ガラスペルジャー12内に導入され
た陽極液は、ガスリフト管17を発生オゾン含有酸素の
上昇によって、従来のようにポンプで強制することなく
循環でき、発生オゾン含有酸素の上部多孔質集電極3面
への停滞を防止する。図示の陽極液循環機構18はガラ
スペルジャー12の中心にガスリフト管17を、周辺に
取入口9を設けたが、逆の配置も採用できることは勿論
である。The upper main anode 2 has an anolyte outlet hole 8 in the center and a plurality of anolyte inlet holes 9 around the periphery, such as an anolyte reservoir with an upper outlet 10 and an anolyte port 11 on the side. It is covered with a container, for example a glass Pel jar 12, which is fixed to the upper main anode 2 with studs 13, so that the anolyte remains at a water level 14, so that the upper porous collector electrode 3 is always below the liquid level. The supply of anolyte to the upper porous collector electrode 3 takes place smoothly, and this porous collector electrode 3 supplies electrical power and diffuses the generated ozone-containing oxygen. Moreover, inside, a base 15 communicates with the anolyte outlet hole 8, and an upper end 16 has a glass Pel jar 12.
A gas lift tube 17 opening into the interior is provided, and the anolyte circulation mechanism 18 is formed by the anolyte inlet hole 9, the upper porous collector electrode 3, the electrolyte outlet hole 8, and the gas lift tube 17.
The anolyte introduced into the glass Pel jar 12 can be circulated through the gas lift tube 17 by raising the generated ozone-containing oxygen without being forced by a pump as in the conventional case. Prevents stagnation on the three surfaces of the porous collector electrode. Although the illustrated anolyte circulation mechanism 18 has the gas lift pipe 17 in the center of the glass pelger 12 and the intake port 9 around the periphery, it is of course possible to adopt the opposite arrangement.
上部主陽極2下面には中心はど深く刻んだ傾斜溝19を
同心状に設け、かつ各溝19は第3図に示すように中心
方向の連絡溝20で連通した発生オゾン含有酸素集合手
段21が形成されている。従って上部多孔質集電極3で
発生したオゾン含有酸素は傾斜溝19を中心に向って流
れ、陽極液出口孔8に達し、ガスリフト管17を陽極液
とともに上昇し、液は循環し、オゾン含有酸素は取出口
10より外部に取出される。On the lower surface of the upper main anode 2, inclined grooves 19 with deep grooves in the center are concentrically provided, and each groove 19 is connected to a generated ozone-containing oxygen collection means 21 through a communication groove 20 in the center direction, as shown in FIG. is formed. Therefore, the ozone-containing oxygen generated in the upper porous collector electrode 3 flows toward the center through the inclined groove 19, reaches the anolyte outlet hole 8, ascends the gas lift tube 17 together with the anolyte, and the liquid circulates, and the ozone-containing oxygen is taken out from the outlet 10.
上記の実施例は水電解によるオゾン含有酸素の発生につ
いて説明したが、塩酸電解によって塩素の発生、その他
臭素などのガス発生用電解にも広く利用できることは勿
論であり、いずれの場合でも発生ガスに十分の耐性をも
つフッ素系イオン交換膜が推奨される。The above example describes the generation of ozone-containing oxygen by water electrolysis, but it can of course also be widely used to generate chlorine by hydrochloric acid electrolysis, and electrolysis for generating other gases such as bromine. Fluorinated ion exchange membranes with sufficient resistance are recommended.
このように本発明においては陽極液は常時陽極側を浸漬
して水切れによる電極の損傷は防止でき、信頼性に富む
とともに、主陽極下面の傾斜溝が酸素、オゾン、塩素、
臭素等の発生ガスの電極からの離脱及び集合を促進して
電解効率を向上させ、かつ陽極液の循環を、ポンプ使用
等の強制装置に代えて発生ガスの上昇力を利用して陽極
液の循環を行うガスリフト管による陽極液循環機構とし
たから故障はなくなり、省エネルギとなり、かつポンプ
の据付面積も省略できるなどその効果は著しい。In this way, in the present invention, the anode side is constantly immersed in the anolyte to prevent damage to the electrode due to water running out, and is highly reliable.
It improves electrolysis efficiency by promoting the separation and collection of generated gases such as bromine from the electrode, and the anolyte circulation is improved by utilizing the rising force of the generated gas instead of using a forced device such as a pump. The anolyte circulation mechanism uses a gas lift tube for circulation, which eliminates malfunctions, saves energy, and eliminates the installation space of the pump, which has remarkable effects.
実験例1
本発明による電解装置を用いて水電解による酸素の製造
実験を行った。Experimental Example 1 An experiment was conducted to produce oxygen by water electrolysis using the electrolyzer according to the present invention.
膜−電極接合体 白金・イリジウム合金を両面に接合
した
ナフィオン117膜
(デュポン社製品)
陽極側集電極 白金メツキチタン材陰極側集電極
多孔質カーボン材
電極有効面積 50cシ
温 度 50〜60℃陽 極
液 水
電 流 50A
電流密度 10QA/d+′
電 圧 1.8 Volt酸素
発生W 9.9Q/hr
電流効率 99%
実験例2
本発明による電解装置を用いて水電解によるオゾンの製
造実験を行った。Membrane-electrode assembly Nafion 117 membrane with platinum-iridium alloy bonded on both sides (DuPont product) Anode side collector electrode Platinum-plated titanium material cathode side collector electrode
Porous carbon material electrode effective area 50℃ Temperature 50-60℃ Anode liquid Water current 50A Current density 10QA/d+' Voltage 1.8 Volt Oxygen generation W 9.9Q/hr Current efficiency 99% Experimental example 2 Invention An experiment was conducted to produce ozone by water electrolysis using an electrolyzer.
膜−電極接合体 陰極側にのみ白金
メツキしたナフィオン
117膜
陽極側集電極 二酸化鉛メツキしたチタン材
陰極側集電極 多孔質カーボン材
電極有効面積 50cIf
温 度 30〜40℃陽 極
液 水
電 流 50A
電流密度 100A/da’
電 圧 3.2 Voltオ
ゾン発生量 1.7g/hr
電流効率 11.4%
実験例3
本発明による電解装置を用いて塩素電解による塩素の製
造実験を行った。Membrane-electrode assembly Nafion 117 membrane anode side collector electrode with platinum plating only on the cathode side Titanium material cathode side collector electrode plated with lead dioxide Porous carbon material electrode effective area 50 cIf Temperature 30-40℃ Anode liquid Water current 50A Current Density: 100 A/da' Voltage: 3.2 Volt Ozone generation amount: 1.7 g/hr Current efficiency: 11.4% Experimental Example 3 An experiment was conducted to produce chlorine by chlorine electrolysis using the electrolyzer according to the present invention.
膜−電極接合体 白金・イリジウム合金を両面に接合
した
ナフィオン117膜
陽極側集電極 イリジウム酸化物を被膜したチタン
材
陰極側集電極 多孔質カーボン材
温 度 30℃
陽 極 液 7n−HCffi電
流 30A
電流密度 80A/da’
電 圧 1.8 Volt塩素
発生m 37.6g/hr
電流効率 95%Membrane-electrode assembly Nafion 117 membrane anode collector electrode with platinum-iridium alloy bonded on both sides Titanium cathode collector electrode coated with iridium oxide Porous carbon material Temperature 30°C Anolyte 7n-HCffi electrode
Current 30A Current density 80A/da' Voltage 1.8 Volt Chlorine generation m 37.6g/hr Current efficiency 95%
第1図は本発明の一実施例における断面図、第2図は要
部の拡大断面図、第3図は第1図の■、■線断面図であ
り、第4図は従来例のフローシートである。
l・・・発生用電解装置 2・・・上部主陽極3・・
・上部多孔質集電極 4・・・固体高分子電解質膜
5・・・下部多孔質集電極 6・・・下部主陰極7・・
・ボルト 訃・・陽極液出口孔9・・・陽
極液取入孔 lO・・・取出口11・・・電解液人
口 12・・・ガラスペルジャー13・・・植込
ボルト 14・・・水 位15・・・基 部
16・・・上 端17・・・ガスリフト管
18・・・電解液循環機構19・・・傾斜溝 2
0・・・連絡溝21・・・発生オゾン含有 22・・
・Oリング酸素集合手段Fig. 1 is a sectional view of one embodiment of the present invention, Fig. 2 is an enlarged sectional view of the main part, Fig. 3 is a sectional view taken along the lines ■ and ■ in Fig. 1, and Fig. 4 is a flowchart of the conventional example. It is a sheet. l... Generation electrolytic device 2... Upper main anode 3...
- Upper porous collector electrode 4... Solid polymer electrolyte membrane 5... Lower porous collector electrode 6... Lower main cathode 7...
- Bolt - Anolyte outlet hole 9... Anolyte intake hole lO... Outlet 11... Electrolyte population 12... Glass Pel jar 13... Studded bolt 14... Water Position 15...Base
16...Top end 17...Gas lift pipe
18... Electrolyte circulation mechanism 19... Inclined groove 2
0...Communication groove 21...Contains generated ozone 22...
・O-ring oxygen collecting means
Claims (3)
固体高分子電解質膜、下部多孔質集 電極、下部主陰極とが積層して形成された ガス発生用電解装置において、上部電極側 に陽極液溜容器を直結して、この陽極を陽 極液中に浸漬させることを特徴とするガス 発生用電解装置。(1) an upper main anode and an upper porous collector electrode in contact with it;
In an electrolytic device for gas generation formed by laminating a solid polymer electrolyte membrane, a lower porous collector electrode, and a lower main cathode, an anode liquid reservoir is directly connected to the upper electrode side, and this anode is immersed in the anolyte liquid. An electrolytic device for gas generation characterized by immersion.
固体高分子電解質膜、下部多孔質集 電極、下部主陰極とが積層して形成された ガス発生用電解装置において、上部電極側 に陽極液溜容器を直結して、上部主陽極に ガスリフト管を備え、離れた位置に複数個 の給液用孔を備えた陽極液循環機構を有す るガス発生用電解装置。(2) an upper main anode and an upper porous collector electrode in contact therewith;
In an electrolytic device for gas generation formed by laminating a solid polymer electrolyte membrane, a lower porous collector electrode, and a lower main cathode, an anode reservoir is directly connected to the upper electrode side, and a gas lift tube is connected to the upper main anode. An electrolytic device for gas generation having an anolyte circulation mechanism with a plurality of liquid supply holes at separate locations.
固体高分子電解質膜、下部多孔質集 電極、下部主陰極とが積層して形成された ガス発生用電解装置において、上部主陽極 の電解室側に溝を加工し、溝の深さを中心 部に向って円錐状の傾斜をもたせた発生ガ ス集合手段を備えたガス発生用電解装置。(3) an upper main anode and an upper porous collector electrode in contact therewith;
In an electrolytic device for gas generation formed by laminating a solid polymer electrolyte membrane, a lower porous collector electrode, and a lower main cathode, a groove is machined on the electrolytic chamber side of the upper main anode, and the depth of the groove is adjusted to the center. An electrolytic device for gas generation equipped with a generated gas collecting means having a conical slope toward.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61246578A JPS63100190A (en) | 1986-10-16 | 1986-10-16 | Electrolytic device for generating gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61246578A JPS63100190A (en) | 1986-10-16 | 1986-10-16 | Electrolytic device for generating gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS63100190A true JPS63100190A (en) | 1988-05-02 |
Family
ID=17150503
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61246578A Pending JPS63100190A (en) | 1986-10-16 | 1986-10-16 | Electrolytic device for generating gas |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63100190A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01312092A (en) * | 1988-06-10 | 1989-12-15 | Sasakura Eng Co Ltd | Production of ozone by electrolysis |
| JPH0290995A (en) * | 1988-09-29 | 1990-03-30 | Permelec Electrode Ltd | Water treatment process and device using electrolytic ozone |
| JPH02259090A (en) * | 1989-03-31 | 1990-10-19 | Sasakura Eng Co Ltd | Production of ozone by electrolysis |
| WO2011160446A1 (en) * | 2010-06-22 | 2011-12-29 | Liu Xun | Water electrolytic device |
| CN105316698A (en) * | 2014-07-31 | 2016-02-10 | 索尔科生物医疗株式会社 | Hydrogen generating unit for producing hydrogen water |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5896886A (en) * | 1981-12-04 | 1983-06-09 | Asahi Glass Co Ltd | Electrolyzing method for aqueous alkali metal salt solution |
| JPS5928635A (en) * | 1982-08-11 | 1984-02-15 | Hitachi Metals Ltd | Measuring method of pressure distribution |
| JPS59200776A (en) * | 1983-04-26 | 1984-11-14 | Kanegafuchi Chem Ind Co Ltd | Electrolyzing method and electrolytic cell used therefor |
-
1986
- 1986-10-16 JP JP61246578A patent/JPS63100190A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5896886A (en) * | 1981-12-04 | 1983-06-09 | Asahi Glass Co Ltd | Electrolyzing method for aqueous alkali metal salt solution |
| JPS5928635A (en) * | 1982-08-11 | 1984-02-15 | Hitachi Metals Ltd | Measuring method of pressure distribution |
| JPS59200776A (en) * | 1983-04-26 | 1984-11-14 | Kanegafuchi Chem Ind Co Ltd | Electrolyzing method and electrolytic cell used therefor |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01312092A (en) * | 1988-06-10 | 1989-12-15 | Sasakura Eng Co Ltd | Production of ozone by electrolysis |
| JPH0290995A (en) * | 1988-09-29 | 1990-03-30 | Permelec Electrode Ltd | Water treatment process and device using electrolytic ozone |
| JPH02259090A (en) * | 1989-03-31 | 1990-10-19 | Sasakura Eng Co Ltd | Production of ozone by electrolysis |
| WO2011160446A1 (en) * | 2010-06-22 | 2011-12-29 | Liu Xun | Water electrolytic device |
| CN105316698A (en) * | 2014-07-31 | 2016-02-10 | 索尔科生物医疗株式会社 | Hydrogen generating unit for producing hydrogen water |
| CN105316698B (en) * | 2014-07-31 | 2018-09-28 | 索尔科生物医疗株式会社 | Hydrogen generation unit for producing hydrogen-rich water |
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