JPS6151636B2 - - Google Patents
Info
- Publication number
- JPS6151636B2 JPS6151636B2 JP58001688A JP168883A JPS6151636B2 JP S6151636 B2 JPS6151636 B2 JP S6151636B2 JP 58001688 A JP58001688 A JP 58001688A JP 168883 A JP168883 A JP 168883A JP S6151636 B2 JPS6151636 B2 JP S6151636B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- plate
- electrolytic cell
- present
- electrolytic
- 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
- 239000000126 substance Substances 0.000 claims description 13
- 229920003002 synthetic resin Polymers 0.000 claims description 10
- 239000000057 synthetic resin Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 9
- 239000003792 electrolyte Substances 0.000 description 10
- 239000004020 conductor Substances 0.000 description 6
- 230000002093 peripheral effect Effects 0.000 description 6
- 125000006850 spacer group Chemical group 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 229920005989 resin Polymers 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000007784 solid electrolyte Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000915 polyvinyl chloride Polymers 0.000 description 2
- 239000004800 polyvinyl chloride Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
Landscapes
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
【発明の詳細な説明】
本発明は電解槽用電極板に関し、さらに詳しく
は導電性物質を含む合成樹脂材料を用いた電解槽
用電極板に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrode plate for an electrolytic cell, and more particularly to an electrode plate for an electrolytic cell using a synthetic resin material containing a conductive substance.
従来、電解液流通孔を設けた合成樹脂板を組合
せ、正極室と負極室を隔膜を介して重ね合せた積
層型電解槽が知られている。第1図はこのような
積層型電解槽の典型例を示すもので、隔膜5と、
枠状スペーサー1と、この隔膜5および枠状スペ
ーサーをはさんで負極側および正極側(一方のみ
図示)にそれぞれ対称形に積層された導電性物質
を含む板状電極3とから構成される。正極液(ま
たは負極液)は、板状電極3の電解液流通孔6A
を通り、その上部のスペーサー1の枠内空間2か
ら電極面上に流れ、他方の枠内空間の流通孔から
外部または次の電解槽に流される。一方、負極液
(または正極液)は、流通孔6Bから隔膜5をは
さんで対称に設置されたスペーサー(図示せず)
の枠内空間から同様に流入され、排出される。 2. Description of the Related Art Conventionally, a stacked electrolytic cell is known in which a positive electrode chamber and a negative electrode chamber are stacked with a diaphragm interposed in between synthetic resin plates provided with electrolyte flow holes. FIG. 1 shows a typical example of such a stacked electrolytic cell, which includes a diaphragm 5,
It is composed of a frame-shaped spacer 1 and a plate-shaped electrode 3 containing a conductive material laminated symmetrically on the negative electrode side and the positive electrode side (only one side is shown) with the diaphragm 5 and the frame-shaped spacer in between. The positive electrode solution (or negative electrode solution) is supplied through the electrolyte flow hole 6A of the plate electrode 3.
It flows from the frame space 2 of the spacer 1 above onto the electrode surface, and then flows to the outside or the next electrolytic cell from the communication hole in the other frame space. On the other hand, the negative electrode liquid (or positive electrode liquid) is supplied through spacers (not shown) installed symmetrically across the diaphragm 5 from the flow hole 6B.
Similarly, it flows in and is discharged from the space within the frame.
上記電解槽に用いる電極板は導電性物質を含有
させることにより電気伝導性を有しているが、こ
のような電極板では、極板全域が電気の良導体の
場合、電解液の流通路部分を通つて電流が電解室
外に漏洩するという欠点がある。このような漏洩
電流は、電解槽の電極間を通る電流ではなく、目
的とする電解反応(または電池反応)に通常関与
せず無効な電力となるものである。 The electrode plate used in the electrolytic cell has electrical conductivity by containing a conductive substance, but in such an electrode plate, if the entire area of the plate is a good conductor of electricity, the electrolyte flow path is The drawback is that current leaks outside the electrolysis chamber. Such leakage current is not a current passing between the electrodes of the electrolytic cell, but is normally not involved in the intended electrolytic reaction (or battery reaction) and becomes ineffective power.
本発明の目的は、上記従来技術の欠点を除去
し、電解槽からの漏洩電流を可及的に小さくする
ことができる電解槽用電極を提供することにあ
る。 An object of the present invention is to provide an electrode for an electrolytic cell that can eliminate the drawbacks of the prior art described above and can reduce leakage current from the electrolytic cell as much as possible.
本発明者らは、電解液流路の電気抵抗を小さく
する要因をできるだけ取り除くため、電解室外の
電解液流路部分の電極板中に含まれる導電性物質
を少なくすることにより、該部分の電気抵抗が増
大し、漏洩電流を小さくすることを見出し、本発
明に到達したものである。 In order to eliminate as much as possible the factors that reduce the electrical resistance of the electrolyte flow path, the present inventors reduced the amount of conductive material contained in the electrode plates in the electrolyte flow path outside the electrolytic chamber, thereby increasing the electrical resistance of the electrolyte flow path. The present invention was achieved by discovering that the resistance increases and the leakage current decreases.
本発明は、導電性物質を含む合成樹脂からなる
電解槽用電極板において、電解室外の液流路部分
の導電性物質の含有率を電解室部分含有率の70%
以下としたことを特徴とする。 The present invention provides an electrode plate for an electrolytic cell made of a synthetic resin containing a conductive substance, in which the content of the conductive substance in the liquid flow path outside the electrolytic chamber is 70% of the content in the electrolytic chamber.
It is characterized by the following.
本発明は、電解槽のみならず、電解槽と同様な
構成の電池にも同様に適用されるので、本明細書
中の電解槽または電極板なる用語は電池または極
板と同義であり、勿論、本特許請求の範囲に含ま
れる。 The present invention applies not only to electrolytic cells but also to batteries having the same configuration as electrolytic cells, so the term electrolytic cell or electrode plate in this specification is synonymous with battery or electrode plate, and of course , within the scope of the claims.
本発明において、樹脂中に含有させる導電性物
質としては炭素粉、金属粉等の電子伝導性物質の
他、正孔やイオンによる伝導性を有するもの、す
なわち各種半導体や固体電解質等があげられる。 In the present invention, examples of the conductive substance contained in the resin include electron conductive substances such as carbon powder and metal powder, as well as substances having hole and ion conductivity, such as various semiconductors and solid electrolytes.
本発明の電極板を形成する合成樹脂は、電極板
を構成し得るものであればどのようなものでもよ
く、例えばポリエチレン、ポリプロピレン、ポリ
塩化ビニル、ポリカーボネート等の合成樹脂や、
シート状に成形可能な鉱物質等の樹脂と同等の性
質を有するものがあげられる。上記合成樹脂中に
含有させる導電性物質の量は、電解または反応を
行なう上で充分な導電性を与える量でよいが、例
えば金属粉等の場合は約50重量%以上である。本
発明において電解室外の電解液流路の周囲を構成
する合成樹脂は導電性物質を含まないことが望ま
しいが、実質的には電気導通部分の70重量%以下
(好ましくは50重量%以下)含んでいても電気抵
抗は充分に大きくなり、本発明の目的を達成する
ことができる。導電性物質は電極室部分では樹脂
中に均一に含有されていることが好ましい。 The synthetic resin forming the electrode plate of the present invention may be any material as long as it can form the electrode plate, such as synthetic resins such as polyethylene, polypropylene, polyvinyl chloride, polycarbonate,
Examples include minerals that can be molded into sheets and have properties similar to resins. The amount of the conductive substance contained in the synthetic resin may be an amount that provides sufficient conductivity for electrolysis or reaction, and in the case of metal powder, for example, it is about 50% by weight or more. In the present invention, it is preferable that the synthetic resin surrounding the electrolyte flow path outside the electrolytic chamber does not contain a conductive substance, but it does not substantially contain 70% by weight or less (preferably 50% by weight or less) of the electrically conductive part. However, the electrical resistance becomes sufficiently large and the object of the present invention can be achieved. It is preferable that the conductive substance is uniformly contained in the resin in the electrode chamber portion.
なお、電極板の製作上は、例えば固体電解質を
多量に含有する合成樹脂は脆くて加工しにくく、
かつボルトなどで締めつけることも困難である
が、電極板の周辺部(電解液流通部)は固体電解
質を多量に含まず、比較的加工しやすいので、製
作上有利であり、強度低下も問題にならない。 In addition, when manufacturing the electrode plate, for example, synthetic resin containing a large amount of solid electrolyte is brittle and difficult to process.
Although it is also difficult to tighten with bolts, etc., the peripheral area of the electrode plate (electrolyte flow area) does not contain a large amount of solid electrolyte and is relatively easy to process, which is advantageous in terms of manufacturing, and strength reduction is also an issue. It won't happen.
以下、本発明を実施例によりさらに詳細に説明
する。 Hereinafter, the present invention will be explained in more detail with reference to Examples.
実施例 1
第2図に示す複極板を積層して電解槽を試作し
た。複極板の合成樹脂シートは、第2図に示すよ
うに液流通孔を含むシート両端部分に炭素粉を中
央部分の40〜60重量%程度含有するフツ素樹脂結
着シートであり、これにスペーサーと隔膜とを重
ねて一つの単電解槽を構成した。この単電解槽を
二個重ね合わせて複極電解槽とした。なお、漏洩
電流測定の際には、隔膜の代わりに軟質のポリ塩
化ビニルシートを用いて隔膜部を電気的に絶縁し
た。電解槽に1モル/塩化ナトリウム水溶液を
満たし、両複極板間の電気抵抗を交流ブリツジ法
および回路試験器で測定した。なお、第2図に示
す両端が灰白色で、ほとんど炭素粉を含まない複
極板を用いた場合と、比較のために複極板全域
に、ほぼ均一の炭素粉を含有するものについて
も、同様に検討した。その結果、複極板の両端部
も中央部と同じく炭素粉を均一に含有する場合の
抵抗を1とすると、40〜60重量%を含む場合は
10、ほとんど含まないものは12であつた。この結
果、電解液流路を通つて流れる漏洩電流は本発明
により、大きく低減されることが明らかになつ
た。Example 1 An electrolytic cell was fabricated by stacking bipolar plates shown in FIG. 2. As shown in Figure 2, the synthetic resin sheet of the bipolar plate is a fluororesin binding sheet that contains carbon powder at both ends of the sheet, including the liquid flow holes, in an amount of 40 to 60% by weight of the central portion. A single electrolytic cell was constructed by stacking the spacer and the diaphragm. Two of these single electrolytic cells were stacked together to form a bipolar electrolytic cell. Note that when measuring leakage current, a soft polyvinyl chloride sheet was used instead of the diaphragm to electrically insulate the diaphragm portion. The electrolytic cell was filled with 1 mol/aqueous sodium chloride solution, and the electrical resistance between both bipolar plates was measured using an AC bridge method and a circuit tester. The same applies to the case of using a bipolar plate shown in Fig. 2, which has grayish-white ends and contains almost no carbon powder, and for comparison, the case of using a bipolar plate containing almost uniform carbon powder over the entire area of the bipolar plate. We considered this. As a result, assuming that the resistance is 1 when both ends of the bipolar plate contain carbon powder uniformly like the center, then when it contains 40 to 60% by weight,
10, and those containing almost no amount were 12. As a result, it has become clear that the leakage current flowing through the electrolyte flow path is significantly reduced by the present invention.
第3図は、本発明の他の実施例を示す複極板の
斜視図であるが、この場合は周辺部の電解液流通
孔10の他に中央部にも流通孔11が形成され、
この中央部の樹脂中の導電性物質の含量も周辺部
のそれと同様に少なくなつている。このような構
成としても、実施例1と同様に漏洩電流を減少さ
せることができる。また流通孔を多く形成して
も、その部分には導電性物質があまり含まれてい
ないので、強度、耐久性等に悪影響を及ぼすこと
がない。 FIG. 3 is a perspective view of a bipolar plate showing another embodiment of the present invention. In this case, in addition to the electrolyte flow holes 10 in the peripheral portion, the flow holes 11 are formed in the central portion,
The content of the conductive substance in the resin in the central portion is also reduced, similar to that in the peripheral portion. Even with such a configuration, leakage current can be reduced similarly to the first embodiment. Furthermore, even if a large number of communication holes are formed, since the conductive material is not contained in those portions, the strength, durability, etc. will not be adversely affected.
以上、本発明によれば、板状電極の液流通孔の
周辺部分は比較的高い電気抵抗をもつため、電極
板の周辺部から導電性枠体、ホルダー、溶液を通
つて流れる漏洩電流を大幅に低減することができ
る。また電極を構成する板状材料の中央部に導電
性物質を多く存在させ、液流通孔等の加工部分の
多い周辺部には導電性物質が少ない(または存在
しない)ので、強度の弱い電極材料(マトリツク
ス材料)でも充分使用可能となり、また耐久性も
向上する。 As described above, according to the present invention, since the peripheral portion of the liquid flow hole of the plate electrode has a relatively high electrical resistance, the leakage current flowing from the peripheral portion of the electrode plate through the conductive frame, the holder, and the solution can be significantly reduced. can be reduced to In addition, a large amount of conductive material is present in the central part of the plate-like material that constitutes the electrode, and there is less (or no) conductive material in the peripheral part where there are many processed parts such as liquid flow holes, so the electrode material has weak strength. (matrix material) can be used satisfactorily, and durability is also improved.
第1図は、本発明の板状電極が用いられる液流
通型電解槽の一例を示す展開図、第2図および第
3図は、それぞれ本発明の一実施例を示す板状電
極の斜視図である。図中の符号1はスペーサー、
3は(板状)電極、5は隔膜、10,11は液流
通孔を示す。
FIG. 1 is a developed view showing an example of a liquid flow type electrolytic cell in which a plate-shaped electrode of the present invention is used, and FIGS. 2 and 3 are perspective views of plate-shaped electrodes each showing an example of the present invention. It is. Code 1 in the figure is a spacer,
3 is a (plate-shaped) electrode, 5 is a diaphragm, and 10 and 11 are liquid flow holes.
Claims (1)
電極板において、電解室外の液流路部分の導電性
物質の含有率を電解室部分の含有率の70%以下と
したことを特徴とする電解槽用電極板。1. An electrode plate for an electrolytic cell made of a synthetic resin containing a conductive substance, characterized in that the content of the conductive substance in the liquid flow path outside the electrolytic chamber is 70% or less of the content in the electrolytic chamber. Electrode plate for tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58001688A JPS59126782A (en) | 1983-01-11 | 1983-01-11 | Electrode plate for electrolytic cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58001688A JPS59126782A (en) | 1983-01-11 | 1983-01-11 | Electrode plate for electrolytic cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59126782A JPS59126782A (en) | 1984-07-21 |
| JPS6151636B2 true JPS6151636B2 (en) | 1986-11-10 |
Family
ID=11508452
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58001688A Granted JPS59126782A (en) | 1983-01-11 | 1983-01-11 | Electrode plate for electrolytic cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59126782A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62200668A (en) * | 1986-02-27 | 1987-09-04 | Agency Of Ind Science & Technol | Battery device |
| JPH0792235A (en) * | 1993-09-25 | 1995-04-07 | Nec Corp | Semiconductor device and method for measuring delay time of the device |
| NL2033470B1 (en) * | 2022-11-06 | 2024-05-24 | Xintc B V | Cell for forming an electrolyser, electrolyser comprising such cell, method for manufacturing and operating an electrolyser |
| CN118996470A (en) * | 2024-10-25 | 2024-11-22 | 爱德曼氢能源装备有限公司 | Forced distribution type polar plate structure and electrolytic tank comprising same |
-
1983
- 1983-01-11 JP JP58001688A patent/JPS59126782A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59126782A (en) | 1984-07-21 |
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