JPS63324Y2 - - Google Patents
Info
- Publication number
- JPS63324Y2 JPS63324Y2 JP18960882U JP18960882U JPS63324Y2 JP S63324 Y2 JPS63324 Y2 JP S63324Y2 JP 18960882 U JP18960882 U JP 18960882U JP 18960882 U JP18960882 U JP 18960882U JP S63324 Y2 JPS63324 Y2 JP S63324Y2
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- hydrogen
- tank
- air
- perforated plate
- 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.)
- Expired
Links
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 21
- 239000003792 electrolyte Substances 0.000 claims description 18
- 239000001257 hydrogen Substances 0.000 claims description 13
- 229910052739 hydrogen Inorganic materials 0.000 claims description 13
- 238000007872 degassing Methods 0.000 claims description 6
- 239000008151 electrolyte solution Substances 0.000 description 6
- 239000003595 mist Substances 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000007865 diluting Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
【考案の詳細な説明】
本考案は電解液を短時間滞留させて、電解液中
の水素を分離する水素ガス抜きタンクの改良に関
する。[Detailed Description of the Invention] The present invention relates to an improvement in a hydrogen degassing tank that retains an electrolytic solution for a short time and separates hydrogen from the electrolytic solution.
従来の水素ガス抜きタンクは第１図に示すよう
に、図示しない電解槽ユニツトから送られてきた
電解液Ａを電解液供給管ａからタンクｂに供給
し、短時間滞留させて水素ガスの自然分離をねら
つていた。しかし充分な分離が得られず、しかも
水素ガス濃度を爆発限界以下に希釈する必要上、
空気Ｂを空気供給口ｃから供給するが送り込む多
量の空気に水素ガスに起因するミスト（粘着性の
泡を含む）がまき上げられ、空気の排出ダクトｅ
の途中に設けられたフレームアレスタｆの金網を
塞ぐ結果となつた。 As shown in Fig. 1, in a conventional hydrogen degassing tank, electrolyte A sent from an electrolyzer unit (not shown) is supplied from an electrolyte supply pipe a to a tank b, where it is allowed to stagnate for a short period of time to naturally release hydrogen gas. They were aiming for separation. However, sufficient separation could not be obtained, and it was necessary to dilute the hydrogen gas concentration to below the explosive limit.
Air B is supplied from the air supply port c, but mist (including sticky bubbles) caused by hydrogen gas is stirred up in the large amount of air sent into the air exhaust duct e.
This resulted in blocking the wire mesh of the flame arrester f, which was installed in the middle.
このため供給する空気量を減らさねばならず水
素ガスの充分な希釈ができなかつた。なおｄは空
気排出口、Ｃは水素ガス抜き後の電解液でｇはそ
の電解液排出管を示す。 For this reason, the amount of air to be supplied had to be reduced, and hydrogen gas could not be diluted sufficiently. Note that d is an air outlet, C is an electrolyte after hydrogen gas has been removed, and g is an electrolyte discharge pipe.
本考案は上記の問題を解決しようとしたもの
で、電解液から水素ガスを効率的に分離し、かつ
供給空気によるミストの同判をなくすことを目的
とする。 The present invention is an attempt to solve the above-mentioned problems, and aims to efficiently separate hydrogen gas from the electrolyte and eliminate mist formation caused by supplied air.
このため、本考案はタンク内に電解液を導入、
滞留させて電解液中の水素を分離する水素ガス抜
きタンクにおいて、タンク内に電解液を導入して
シヤワ状にふらせる多孔管と同多孔管の上下に
夫々多孔板を配設すると共に上側多孔板の上部で
かつ多孔板と平行に空気供給口を設けたことに特
徴を有するものである。 For this reason, the present invention introduces electrolyte into the tank.
In a hydrogen degassing tank that separates hydrogen in an electrolytic solution by retaining it, a perforated tube is installed to introduce the electrolytic solution into the tank and make it sway, and a perforated plate is installed above and below the same porous tube, and an upper porous The feature is that an air supply port is provided at the top of the plate and parallel to the perforated plate.
以下本考案の好ましい実施例について第２図を
用いて説明する。 A preferred embodiment of the present invention will be described below with reference to FIG.
Ａは電解液、１は多孔管である。タンク内に収
納されている部分は多数の孔が明けられており、
ここから電解液をシヤワ状にふらせる。 A is an electrolytic solution, and 1 is a porous tube. The part stored inside the tank has many holes,
From here, sprinkle the electrolyte.
８は多孔管１の下側に配設された多孔板、９は
多孔管１の上側に設けられた多孔板である。Ｂは
空気を示し空気供給口３はタンク２の横方向に設
けられている。 8 is a perforated plate disposed below the perforated pipe 1, and 9 is a perforated plate provided above the perforated pipe 1. B indicates air, and the air supply port 3 is provided in the lateral direction of the tank 2.
つまり、空気Ｂは多孔板９と略々平行になるよ
うに供給される。 That is, the air B is supplied so as to be substantially parallel to the perforated plate 9.
４は空気排出管、５は空気の排出ダクト、６は
フレームアレスタ、７は電解液排出管でＣは水素
ガス抜き後の電解液を夫々示す。 4 is an air discharge pipe, 5 is an air discharge duct, 6 is a flame arrester, 7 is an electrolyte discharge pipe, and C indicates the electrolyte after hydrogen gas has been removed.
図示しない電解槽ユニツトから導入された電解
液Ａは多孔管１からタンク２内にシヤワ状に噴霧
される。多孔管１の下側に配設した多孔板上に電
解液の薄い層を形成しつつ、電解液中の水素を分
離する。そして分離された水素はタンク２内を上
昇する。 Electrolytic solution A introduced from an electrolytic cell unit (not shown) is sprayed into a tank 2 from a porous pipe 1 in a shower shape. Hydrogen in the electrolyte is separated while forming a thin layer of the electrolyte on a perforated plate disposed below the porous tube 1. The separated hydrogen then rises within the tank 2.
水素希釈のための空気Ｂは多孔管１の上側に配
設した多孔板９と平行に供給されるので、噴霧さ
れた電解液Ａが直接空気に触れるのを防ぎ、粘着
性の泡を含むミストが空気排出孔から逃げること
は極めて少ない。したがつてミストがフレームア
レスタ６を塞ぐようなことはない。 Air B for diluting hydrogen is supplied parallel to the perforated plate 9 placed above the perforated tube 1, preventing the sprayed electrolyte A from coming into direct contact with the air and creating a mist containing sticky bubbles. It is extremely rare for the air to escape from the air outlet. Therefore, the mist will not block the flame arrester 6.
一方水素を分離した電解液Ｃは電解液排出管７
から系外へ排出される。 On the other hand, the electrolyte C from which hydrogen has been separated is discharged from the electrolyte discharge pipe 7.
is discharged from the system.
以上詳述したように本考案によれば、従来装置
に比べて電解液中の水素が効率良く分離され、か
つ希釈空気によるミストの同判がないので、ミス
トがフレームアレスタを塞ぐようなことがないな
どの効果を有する。 As detailed above, according to the present invention, hydrogen in the electrolyte is separated more efficiently than in conventional devices, and there is no mist formation caused by diluted air, so there is no possibility of mist blocking the flame arrester. It has the effect of not having any effect.
第１図は従来の水素ガス抜きタンクを表す縦断
面図、第２図は本考案の一実施例を示す縦断面図
である。
１…多孔管、２…タンク、３…空気供給口、
８・９…多孔板。
FIG. 1 is a longitudinal sectional view showing a conventional hydrogen degassing tank, and FIG. 2 is a longitudinal sectional view showing an embodiment of the present invention. 1... Porous pipe, 2... Tank, 3... Air supply port,
8/9...Perforated plate.
Claims (1)
水素を分離する水素ガス抜きタンクにおいて、タ
ンク内に電解液を導入してシヤワ状にふらせる多
孔管と同多孔管の上下に夫々多孔板を配設すると
共に上側多孔板の上部でかつ多孔板と平行に空気
供給口を設けたことを特徴とする水素ガス抜きタ
ンク。 In the hydrogen gas degassing tank, where the electrolyte is introduced into the tank and left there to separate the hydrogen in the electrolyte, there is a perforated tube that introduces the electrolyte into the tank and causes it to sway, and a perforated plate above and below the same porous tube. A hydrogen degassing tank characterized in that an air supply port is provided above the upper perforated plate and parallel to the perforated plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18960882U JPS5993703U (en) | 1982-12-15 | 1982-12-15 | Hydrogen degassing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18960882U JPS5993703U (en) | 1982-12-15 | 1982-12-15 | Hydrogen degassing tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5993703U JPS5993703U (en) | 1984-06-26 |
| JPS63324Y2 true JPS63324Y2 (en) | 1988-01-07 |
Family
ID=30408756
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18960882U Granted JPS5993703U (en) | 1982-12-15 | 1982-12-15 | Hydrogen degassing tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5993703U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016526250A (en) * | 2013-05-02 | 2016-09-01 | ローベルト ボツシユ ゲゼルシヤフト ミツト ベシユレンクテル ハフツングＲｏｂｅｒｔ Ｂｏｓｃｈ Ｇｍｂｈ | Fluid distributor, fuel cell or electrolytic cell, and method of operating fluid distributor |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6912557B2 (en) * | 2017-03-31 | 2021-08-04 | 旭化成株式会社 | Water electrolysis system, water electrolysis method, hydrogen production method |
| JP7808017B2 (en) * | 2022-11-09 | 2026-01-28 | カナデビア株式会社 | Degassing device |
-
1982
- 1982-12-15 JP JP18960882U patent/JPS5993703U/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016526250A (en) * | 2013-05-02 | 2016-09-01 | ローベルト ボツシユ ゲゼルシヤフト ミツト ベシユレンクテル ハフツングＲｏｂｅｒｔ Ｂｏｓｃｈ Ｇｍｂｈ | Fluid distributor, fuel cell or electrolytic cell, and method of operating fluid distributor |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5993703U (en) | 1984-06-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4421534A (en) | Tower for removing odors from gases | |
| MX9604680A (en) | Electrode cap with integral tank cover for acid mist collection. | |
| ATE34728T1 (en) | DEVICE FOR ELECTROCHEMICAL OXYGEN REMOVAL FROM WATER. | |
| KR101143088B1 (en) | Method for the Electrolysis of an Aqueous Solution of Hydrogen Chloride or Chloralkali | |
| CN218573072U (en) | Novel waste gas buffer tank | |
| US2846384A (en) | Bipolar electrolyser | |
| CN223988281U (en) | Horizontal gas processor suitable for alkaline water electrolysis hydrogen production process | |
| CN221618992U (en) | Air purifying device for construction | |
| CN220855831U (en) | Waste gas monitoring alarm for guanidine carbonate production | |
| CN211706326U (en) | Residue dust removal processing apparatus for industrial desulfurization | |
| CN218879585U (en) | Hydrazine hydrate production wastewater treatment device | |
| JPS5993703U (en) | Hydrogen degassing tank | |
| JPS5466376A (en) | Removing apparatus for malodor | |
| JPS5839830Y2 (en) | Drop type water tank with built-in ion exchange resin | |
| JPS61272540A (en) | Ultrasonic wave moisture applying device | |
| JPH09324288A (en) | Hydrogen oxygen generator | |
| SU947224A1 (en) | Electrolyzer for producing oxygen from air water vapour | |
| JPS5544352A (en) | Electrodialytic method | |
| CA2191625A1 (en) | A process for the electrolytic separation of oxygen from its mixtures and equipment to perform this process | |
| JPS61159026U (en) | ||
| JPS58165257A (en) | Electrolyte leak prevention fuel cell | |
| SU571527A1 (en) | Electrolizer for electrochemical treatment of gold-containing etching solutions | |
| JPS5337015A (en) | Color developer regeneration method | |
| JPS59176631U (en) | Wet deodorization equipment | |
| JPS62124224U (en) |