JPS608309B2 - water electrolysis device - Google Patents
water electrolysis deviceInfo
- Publication number
- JPS608309B2 JPS608309B2 JP52080546A JP8054677A JPS608309B2 JP S608309 B2 JPS608309 B2 JP S608309B2 JP 52080546 A JP52080546 A JP 52080546A JP 8054677 A JP8054677 A JP 8054677A JP S608309 B2 JPS608309 B2 JP S608309B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- electrodes
- positive
- hollow part
- porous
- 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
- 238000005868 electrolysis reaction Methods 0.000 title claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 8
- 239000011148 porous material Substances 0.000 claims 2
- 239000007789 gas Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 229910001882 dioxygen Inorganic materials 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000000605 extraction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000004904 shortening Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012510 hollow fiber Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
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)
Description
【発明の詳細な説明】 本発明は電気分解装置の小型化改良に関する。[Detailed description of the invention] The present invention relates to improvements in miniaturization of electrolyzers.
さらに詳しくは電気分解により発生する気体を電極内部
に取出すことにより電極表面での気泡の発生を押えて電
極間距離を短かくする方法に関するものである。電気分
解装置には大きく分けて単極型と複極型があるが、いづ
れの場合にも電極の間に隔膜が設置され隔膜に連なった
ガス室からガスが取出されるようになっている。More specifically, the present invention relates to a method of shortening the distance between electrodes by suppressing the generation of bubbles on the electrode surface by extracting gas generated by electrolysis into the electrode. Electrolyzers are broadly divided into monopolar and bipolar types, but in either case, a diaphragm is installed between the electrodes, and gas is taken out from a gas chamber connected to the diaphragm.
このような構造の場合電流効率を高め併せて装置の小型
化を計る場合に電極間の抵抗を低くする手段が考えられ
る。電極間の抵抗を低くする方法として電極面積を広く
することは電解槽が大きくなり、装置の小型化に逆行す
るばかりか設備費がかさむ。したがって電極間の距離を
短かくする方法が考えられるがこれには電極間の短絡の
危険性の増大と特に電解により発生する泡の含有率が増
大して電極間抵抗が高くなって効果が上らない。泡のス
ムースな除去と電気抵抗を少なくするために粗な隔膜を
用いると、隔膜を通して互いの気体が混合して気体純度
が低下する。さらに電極間の短絡の危険性も増大する。
本発明者は以上のような従釆装置の欠陥を電極間の距離
を短か〈し得る新しい方法を見出して解決した。本発明
は電解によって発生する気体を電解の場から速やかに取
除く機能を備えた装置である。即ち、内部が中空状にな
った多孔質電極を用いて、電極面において発生する気体
が電極内部の中空部を通って取出されるようにした構造
の電気分解装置である。次に図面により水の電気分解を
例としてさらに詳細に説明する。In the case of such a structure, if the current efficiency is to be increased and at the same time the device is to be miniaturized, it is possible to consider means of lowering the resistance between the electrodes. Increasing the area of the electrodes as a method of lowering the resistance between the electrodes increases the size of the electrolytic cell, which not only goes against the trend of miniaturizing the device but also increases equipment costs. Therefore, a method of shortening the distance between the electrodes has been considered, but this increases the risk of short circuit between the electrodes and, in particular, increases the content of bubbles generated by electrolysis, which increases the resistance between the electrodes, making it less effective. No. If a rough diaphragm is used to smoothly remove bubbles and reduce electrical resistance, gases will mix with each other through the diaphragm, resulting in a decrease in gas purity. Furthermore, the risk of short circuit between the electrodes also increases.
The inventor of the present invention solved the above-mentioned defects of the follower device by discovering a new method for shortening the distance between the electrodes. The present invention is a device having a function of quickly removing gas generated by electrolysis from the electrolytic field. That is, the electrolyzer has a structure in which a porous electrode having a hollow interior is used so that gas generated on the electrode surface is taken out through the hollow inside the electrode. Next, water electrolysis will be explained in more detail using the drawings as an example.
第1図は本発明の一例を示す模式図である。1は電解槽
、2は多孔質負電極、3は多孔質正電極、4は電極間に
設置された多孔質隔膜、5は電解槽の蓋、6は20%苛
性ソーダ電解液、7は多孔質電極の内部中空部、8は水
素ガス取出通路及び負電位供給体、9は酸素ガス取出適
路及び正電位供給体、10は水の供給路を示す。FIG. 1 is a schematic diagram showing an example of the present invention. 1 is an electrolytic tank, 2 is a porous negative electrode, 3 is a porous positive electrode, 4 is a porous diaphragm installed between the electrodes, 5 is a lid of the electrolytic tank, 6 is a 20% caustic soda electrolyte, and 7 is a porous In the internal hollow part of the electrode, 8 is a hydrogen gas extraction passage and a negative potential supply body, 9 is an oxygen gas extraction passage and a positive potential supply body, and 10 is a water supply passage.
第2図は従来法を示す模式図である。1は電解槽、2は
負電極、3は正電極、4は電極間に設置された多孔質隔
膜、5は電解槽の蓋、6,7の部分には20%苛性ソー
ダ電解液、8は水素ガス出口、9は酸素ガス出口、10
は負の電位供給路、11は正の電位供給路、12は水の
供給口を示す。FIG. 2 is a schematic diagram showing a conventional method. 1 is an electrolytic tank, 2 is a negative electrode, 3 is a positive electrode, 4 is a porous diaphragm installed between the electrodes, 5 is a lid of the electrolytic tank, 6 and 7 are 20% caustic soda electrolyte, 8 is hydrogen Gas outlet, 9 is oxygen gas outlet, 10
11 is a negative potential supply path, 11 is a positive potential supply path, and 12 is a water supply port.
第2図の装置で電気分解が開始されると2の負電極の表
面に水素ガスが発生し、気泡となって2の負電極と4の
隔膜の間の6を上昇して8の出口へ向う、同様に酸素ガ
スは7を上昇して9の出口へ向う。したがって電気抵抗
を低くしようとして6及び7の隙間を狭くすると、該隙
間において電解液中に占める気体の割合が大きくなって
電極間抵抗が高くなって効果が上らない。又、同じく電
気抵抗を低くするために隔膜を粗な構造のものにすると
、6の部分の水素ガスの気泡と7の部分の酸素ガスの気
泡が相互に混り合って気体の純度が低下する。本発明に
おいては第1図に示されたように電極が多孔質でありし
かもその内部に中空部7があって該中空部7が気体の取
出通路8,9に通じている。When electrolysis starts in the device shown in Figure 2, hydrogen gas is generated on the surface of the negative electrode 2, forms bubbles, rises through 6 between the negative electrode 2 and the diaphragm 4, and reaches the outlet 8. Similarly, oxygen gas rises through 7 and heads toward the exit at 9. Therefore, if the gap between 6 and 7 is narrowed in an attempt to lower the electrical resistance, the proportion of gas in the electrolytic solution in the gap increases, and the inter-electrode resistance increases, making the effect less effective. Similarly, if the diaphragm is made to have a rough structure in order to lower the electrical resistance, the hydrogen gas bubbles at 6 and the oxygen gas bubbles at 7 will mix with each other, reducing the purity of the gas. . In the present invention, as shown in FIG. 1, the electrode is porous and has a hollow portion 7 therein, which communicates with gas extraction passages 8 and 9.
電解により生じる電極表面の気泡は多孔質電極2の隙間
を通って内部の中空部7へ押しやられ、電極と隅膜の間
での気泡の浮遊はなくなる。したがって電極間に設置さ
れた隔膜4は正,負両電極に生じた気体の混合による不
純化を気にすることなく、電極間の短絡と電解液のスム
ースな供給にのみ注意をすればよく、電極間の距離を短
かくすることが可能となった。即ち、隔膜としては目の
荒い不織布のようなものも使用可能であり、隔膜が直接
電極に接触する状態で使用されることも可能である。ま
た操作が理想的に行われれば隔膜を使用しなくても良い
こともあり得る。実際の運転に当っては電極の中空部分
よりも電解液側の圧力を高くするのが好ましい。高くす
ることにより発生する気体はスムースに電極内に導入さ
れる。本発明の特徴である多孔質電極の形状としては例
えば断面図として第3図〜第5図に示したような平板状
で内部の中空部分が種々変ったもの、第6図ィ〜ハにそ
の断面図を示したような多孔質の導電性中空繊維状もし
くはパイプ状のものが用いられる。Air bubbles on the electrode surface generated by electrolysis are pushed through the gap in the porous electrode 2 into the internal hollow part 7, and air bubbles no longer float between the electrode and the corneal membrane. Therefore, the diaphragm 4 installed between the electrodes only needs to be careful about short-circuiting between the electrodes and smooth supply of the electrolyte, without worrying about impurity due to the mixing of gases generated at both the positive and negative electrodes. It became possible to shorten the distance between the electrodes. That is, a material such as a coarse nonwoven fabric can be used as the diaphragm, and it is also possible to use the diaphragm in direct contact with the electrode. Furthermore, if the operation is performed ideally, there may be no need to use a diaphragm. In actual operation, it is preferable to make the pressure on the electrolyte side higher than on the hollow part of the electrode. The gas generated by increasing the height is smoothly introduced into the electrode. Examples of the shape of the porous electrode, which is a feature of the present invention, include flat plate shapes with various internal hollow parts as shown in cross-sectional views in FIGS. 3 to 5, and those shown in FIGS. A porous conductive hollow fiber or pipe shape as shown in the cross-sectional view is used.
電極の多孔質化の方法としては、一般の暁給金属の製法
や多孔質カーボンの製法に準ずればよく、又、金属や炭
素の多孔質体を用いて加工することも出来る。従って、
粉体を焼結したものや、金属不織布とか、金鋼を蛾結し
たもの、さらには特閥昭51−99122に示されたよ
うに金属粉末を含む高分子を暁結する方法や炭素材原料
のピッチ、塩ビ、ポリアクリロニトリル系ポリマー、セ
ルロース、その他の高分子材料にガラスの粉末を混入し
ておき耐炎処理、炭素化を行った後、炭化珪素か気化す
る温度で焼成する方法等によっても得ることが出来る。The method for making the electrode porous may be similar to the general manufacturing method for Akatsuki metal or porous carbon, and it is also possible to process it using a porous body of metal or carbon. Therefore,
Sintered powders, metal non-woven fabrics, metal-bonded materials, and methods for sintering polymers containing metal powders as shown in Tokubatsu 1989-99122, and carbon material raw materials. It can also be obtained by mixing glass powder with pitch, PVC, polyacrylonitrile polymer, cellulose, or other polymeric materials, subjecting it to flameproofing and carbonization, and then firing it at a temperature that vaporizes silicon carbide. I can do it.
第1図は本発明による装置の一例を示す。
第2図は従来装置の例を示す。第3,4,5図は本発明
に用いられる平板状電極の断面の例を示す。第6図は中
空繊維状もしくはパイプ状電極の断面の例を示す。第1
図
第2図
第3図
第4図
第5図
第6図FIG. 1 shows an example of a device according to the invention. FIG. 2 shows an example of a conventional device. 3, 4, and 5 show examples of cross sections of flat electrodes used in the present invention. FIG. 6 shows an example of a cross section of a hollow fiber or pipe electrode. 1st
Figure 2 Figure 3 Figure 4 Figure 5 Figure 6
Claims (1)
の供給口及び生成気体取出口を有する水の電気分解装置
において、気体取出口につながる中空部を有し、該中空
部と外部表面とが多くの細孔によって気体の流路を形成
してなる多孔質電極を正負電極とし、電気分解時に電極
面において発生する気体が該電極の細孔を通って中空部
に達し、さらに電解槽の外に取り出されるようにした減
圧もしくは吸引手段を有することを特徴とする水の電気
分解装置。1. A water electrolyzer having an electrolytic cell, positive and negative electrodes, a positive and negative potential supplier to each electrode, a water supply port, and a generated gas outlet, which has a hollow part connected to the gas outlet, and has a hollow part connected to the outside. The positive and negative electrodes are porous electrodes with many pores forming gas flow paths on the surface, and the gas generated on the electrode surface during electrolysis passes through the pores of the electrode and reaches the hollow part, and further electrolysis occurs. 1. A water electrolysis device characterized by having a pressure reduction or suction means for taking out the water out of the tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52080546A JPS608309B2 (en) | 1977-07-06 | 1977-07-06 | water electrolysis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52080546A JPS608309B2 (en) | 1977-07-06 | 1977-07-06 | water electrolysis device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5415475A JPS5415475A (en) | 1979-02-05 |
| JPS608309B2 true JPS608309B2 (en) | 1985-03-01 |
Family
ID=13721332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52080546A Expired JPS608309B2 (en) | 1977-07-06 | 1977-07-06 | water electrolysis device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS608309B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2309978A (en) * | 1996-02-09 | 1997-08-13 | Atraverda Ltd | Titanium suboxide electrode; cathodic protection |
| WO1998051842A1 (en) * | 1997-05-12 | 1998-11-19 | Satoru Miyata | Separate-type hydrogen gas and oxygen gas generator |
-
1977
- 1977-07-06 JP JP52080546A patent/JPS608309B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5415475A (en) | 1979-02-05 |
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