JPH0534623B2 - - Google Patents

Info

Publication number
JPH0534623B2
JPH0534623B2 JP62026975A JP2697587A JPH0534623B2 JP H0534623 B2 JPH0534623 B2 JP H0534623B2 JP 62026975 A JP62026975 A JP 62026975A JP 2697587 A JP2697587 A JP 2697587A JP H0534623 B2 JPH0534623 B2 JP H0534623B2
Authority
JP
Japan
Prior art keywords
concentration
aqueous solution
water
exchange resin
membrane
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 - Lifetime
Application number
JP62026975A
Other languages
Japanese (ja)
Other versions
JPS63195558A (en
Inventor
Shuji Hitomi
Hisashi Kudo
Juko Fujita
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.)
Japan Storage Battery Co Ltd
Original Assignee
Japan Storage Battery 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 Japan Storage Battery Co Ltd filed Critical Japan Storage Battery Co Ltd
Priority to JP62026975A priority Critical patent/JPS63195558A/en
Publication of JPS63195558A publication Critical patent/JPS63195558A/en
Publication of JPH0534623B2 publication Critical patent/JPH0534623B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は水溶液中の溶質の濃度を測定する方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for measuring the concentration of a solute in an aqueous solution.

従来の技術 水溶液中の溶質の濃度を測定する方法として
は、従来、化学分析法あるいは原子吸光分析やイ
オンクロマトグラフ等の機器分析法が実施されて
いる。また、より簡便な方法として、例えば浮子
式比重計が用いられることがある。
BACKGROUND ART Conventionally, chemical analysis methods or instrumental analysis methods such as atomic absorption spectrometry and ion chromatography have been used to measure the concentration of solutes in aqueous solutions. Furthermore, as a simpler method, for example, a float type hydrometer may be used.

発明が解決しようとする問題点 しかるに、上記の化学分析法および機器分析法
は一般に手間がかかるし、大掛りな装置を必要と
する等の問題点があり、さらに、測定の際には対
象とする水溶液を消費したり、その濃度を変化さ
せてしまう等の問題がある。また、浮子式比重計
にしても、その操作は煩雑であるし、連続的に溶
質の濃度を測定しようとする場合には不適当であ
る等の問題があつた。
Problems to be Solved by the Invention However, the above-mentioned chemical analysis methods and instrumental analysis methods are generally time-consuming and have problems such as requiring large-scale equipment. There are problems such as consuming the aqueous solution and changing its concentration. Further, even when using a float type hydrometer, there are problems such as its operation is complicated and it is unsuitable when attempting to continuously measure the concentration of solute.

問題点を解決するための手段 本発明はイオン交換樹脂膜の片面に陰極を、他
面に陽極を一体に接合又は圧接してなる接合体又
は圧接体を撥水性プラスチツク膜で被覆してなる
電気化学セルを用い、これを被測定水溶液中に浸
漬して陰・陽極間に直流の定電圧を印加した際、
前記イオン交換樹脂膜に吸収される水の電気分解
に伴なつて流れる電流が被測定水溶液の溶質の濃
度に対応する水蒸気圧に実質的に正比例するとい
う関係を利用して、水溶液中の溶質の濃度を測定
するものであり、この時、上記水の電気分解に伴
なつて発生する水素と酸素を混合し、電極の触媒
媒用を利用して水に戻すことにより、水溶液を消
費したり、その濃度を変化させることなく連続的
に測定可能な方法を提供するものである。
Means for Solving the Problems The present invention provides an electrical appliance in which a bonded body or pressure-bonded body formed by integrally bonding or press-bonding a cathode on one side of an ion exchange resin membrane and an anode on the other side is covered with a water-repellent plastic membrane. When a chemical cell is immersed in the aqueous solution to be measured and a constant DC voltage is applied between the anode and cathode,
The concentration of solutes in an aqueous solution can be determined by utilizing the relationship that the current flowing as a result of electrolysis of water absorbed by the ion exchange resin membrane is substantially directly proportional to the water vapor pressure corresponding to the concentration of solute in the aqueous solution to be measured. It measures the concentration, and at this time, the hydrogen and oxygen generated during the electrolysis of the water are mixed and returned to water using the catalyst medium of the electrode, thereby consuming the aqueous solution. The present invention provides a method that allows continuous measurement without changing the concentration.

作 用 イオン交換樹脂膜に陰極および陽極をそれぞれ
一体に接合又は圧接してなる電気化学セルのイオ
ン交換樹脂膜に水を吸収させ、陰・陽両極間に直
流電流を通電すると、イオン交換樹脂膜が電解質
として作用し、イオン交換樹脂膜中の水が電気分
解される。イオン交換樹脂膜として水素イオン導
電体としてのカチオン交換膜を用いた場合には次
の反応が起る。
Action When water is absorbed into the ion exchange resin membrane of an electrochemical cell in which a cathode and an anode are integrally bonded or pressure-bonded to an ion exchange resin membrane, and a direct current is passed between the anode and anode electrodes, the ion exchange resin membrane acts as an electrolyte, and the water in the ion exchange resin membrane is electrolyzed. When a cation exchange membrane as a hydrogen ion conductor is used as the ion exchange resin membrane, the following reaction occurs.

陰 極:2H++2e→H2 ……(1) 陽 極:H2O→1/2O2+2H++2e ……(2) 全反応:H2O→H2+1/2O2 ……(3) また、イオン交換樹脂膜として水酸化イオン導
電体としてのアニオン交換膜を用いた場合には次
の反応が起る。
Cathode: 2H + +2e→H 2 ...(1) Anode: H 2 O→1/2O 2 +2H + +2e ...(2) Total reaction: H 2 O→H 2 +1/2O 2 ...(3 ) Furthermore, when an anion exchange membrane as a hydroxide ion conductor is used as the ion exchange resin membrane, the following reaction occurs.

陰 極:2H2O+2e→H2+2OH- ……(1′) 陽 極:2OH-→1/2O2+H2O ……(2′) 全反応:H2O→H2+1/2O2 ……(3′) このような電気化学セルを撥水性プラスチツク
膜で被覆したものを水溶液に浸漬すると、その水
溶液中の水分だけが蒸気となつて撥水性プラスチ
ツク膜を透過し、イオン交換樹脂膜に吸収され
る。従つて、この電気化学セルの陰・陽両極間に
直流電流を通すと、やはりイオン交換樹脂膜に吸
収された水の電気分解が起る。また、陰・陽両極
間に直流の定電圧を印加した場合には、陰・陽両
極間に流れる電流は上記水溶液の水蒸気圧にほぼ
正比例する。従つて、この関係を利用して水溶液
の濃度を測定することができる。
Cathode: 2H 2 O + 2e → H 2 + 2OH - ... (1') Anode: 2OH - →1/2O 2 +H 2 O ... (2') Total reaction: H 2 O → H 2 + 1/2O 2 ... ...(3') When such an electrochemical cell coated with a water-repellent plastic membrane is immersed in an aqueous solution, only the water in the aqueous solution turns into steam and passes through the water-repellent plastic membrane, forming an ion-exchange resin membrane. Absorbed. Therefore, when a direct current is passed between the anode and anode electrodes of this electrochemical cell, electrolysis of the water absorbed in the ion exchange resin membrane also occurs. Furthermore, when a constant DC voltage is applied between the anode and anode electrodes, the current flowing between the anode and anode electrodes is approximately directly proportional to the water vapor pressure of the aqueous solution. Therefore, the concentration of an aqueous solution can be measured using this relationship.

しかし、対象とする水溶液の溶質の濃度を測定
するに当り、上記水の電気分解に伴ない水溶液を
消費することになり、その溶質の濃度は測定時間
の経過と共に高くなる。また、陰極より水素、陽
極より酸素が発生するので大変危険でもあり、密
閉容器中で測定する場合には容器の内圧が上昇す
る等の問題がある。
However, in measuring the solute concentration of the target aqueous solution, the aqueous solution is consumed as the water is electrolyzed, and the solute concentration increases with the passage of measurement time. Furthermore, hydrogen is generated from the cathode and oxygen is generated from the anode, which is very dangerous, and when measuring in a closed container, there are problems such as an increase in the internal pressure of the container.

本発明では水の電気分解により発生した水素と
酸素を、予めそれらが混ざり合うことができるよ
うな空間または通路を設けておいて、陰極か陽極
のいずれか一方、あるいは両極の電極表面上で電
極の触媒作用を利用して再び水に戻す方法を用い
ている。
In the present invention, a space or passage is provided in advance so that hydrogen and oxygen generated by water electrolysis can be mixed, and then the hydrogen and oxygen generated by water electrolysis are placed between the electrodes at either the cathode or the anode, or on the surface of both electrodes. The method uses the catalytic action of water to turn it back into water.

この場合、前記全反応(3)および(3′)は下記の
様になり、生成された水は撥水性プラスチツク膜
を通して水溶液中に戻されるので、上記の如き問
題は解決され、対象とする水溶液を消費したり、
その濃度を変化させることなく連続的な測定が可
能となる。
In this case, the above-mentioned overall reactions (3) and (3') are as follows, and the produced water is returned to the aqueous solution through the water-repellent plastic membrane, so the above problems are solved and the target aqueous solution is consume or
Continuous measurement is possible without changing the concentration.

全反応:H2O→(H2+1/2O2→)H2O ……(4) 尚、電気化学セルを撥水性プラスチツク膜で被
覆するのは、測定の対象となる水溶液がイオン交
換樹脂膜に直接接触すると、水溶液の濃度にあま
り関係なく、ほぼ一定の電流が流れたり、また、
溶質によつては水の電気分解の代りに溶質自体の
電気分解が起るため、水溶液の濃度を測定するこ
とができないからである。
Total reaction: H 2 O → (H 2 +1/2O 2 →) H 2 O ……(4) The reason why the electrochemical cell is covered with a water-repellent plastic membrane is because the aqueous solution to be measured is an ion exchange resin. When in direct contact with the membrane, a nearly constant current flows, regardless of the concentration of the aqueous solution;
This is because, depending on the solute, electrolysis of the solute itself occurs instead of electrolysis of water, making it impossible to measure the concentration of the aqueous solution.

本発明に用いるイオン交換樹脂膜としては、パ
ーフルオロカーボンを樹脂骨格とし、スルフオン
酸基をイオン交換基として保有するカチオン交換
膜が最も優れているが、水酸基を有するアニオン
交換膜を用いてもよい。また、イオン交換樹脂膜
の樹脂骨格としてスチレン−ジビニルベンゼン共
重合体の如き炭化水素系のものを用いてもよい。
また電極はイオン交換樹脂膜と一体に接合しても
よいし、網状または多孔性の電極を圧接してもよ
い。また電極はイオン交換樹脂膜の両面に配して
もよいし、片面だけに配設してもよい。
As the ion exchange resin membrane used in the present invention, a cation exchange membrane having a perfluorocarbon resin skeleton and a sulfonic acid group as an ion exchange group is most suitable, but an anion exchange membrane having a hydroxyl group may also be used. Furthermore, a hydrocarbon type material such as styrene-divinylbenzene copolymer may be used as the resin skeleton of the ion exchange resin membrane.
Further, the electrode may be integrally joined to the ion exchange resin membrane, or a mesh-like or porous electrode may be pressed into contact with the ion exchange resin membrane. Further, the electrodes may be arranged on both sides of the ion exchange resin membrane, or only on one side.

イオン交換樹脂膜への電極の接合方法として
は、所謂無電解メツキ法あるいは触媒粉末と結着
剤との混合物をホツトプレスするホツトプレス法
が適用可能である。電極材料としては白金族金属
などが使用可能である。また電気化学セルを被覆
する撥水性プラスチツク膜材料としては、フツ素
樹脂が最も優れているが、ポリ塩化ビニル、ポリ
プロピレン、ポリエチレンなども使用可能であ
る。撥水性プラスチツク膜は多孔性であることが
望ましいが、非多孔性でもよいことがある。
As a method for joining the electrode to the ion exchange resin membrane, a so-called electroless plating method or a hot pressing method in which a mixture of catalyst powder and a binder is hot pressed can be applied. Platinum group metals and the like can be used as electrode materials. Further, as the material for the water-repellent plastic film covering the electrochemical cell, fluororesin is the best material, but polyvinyl chloride, polypropylene, polyethylene, etc. can also be used. Although it is desirable that the water-repellent plastic membrane be porous, it may also be non-porous.

本発明測定方法は、特に鉛蓄電池の硫酸の濃
度、尿中の塩分などを測定する上で効果的であ
る。
The measuring method of the present invention is particularly effective in measuring the concentration of sulfuric acid in lead-acid batteries, the salt content in urine, and the like.

実施例 以下、本発明のいくつかの実施例について詳述
する。
Examples Some examples of the present invention will be described in detail below.

[実施例 1] パーフルオロカーボンスルホン酸樹脂膜(デユ
ポン製 ナフイオン117)の両面に白金(4mg/
cm2)を無電解メツキ法により接合し、外径10mm,
内径5mmのドーナツ状のイオン交換樹脂膜−触媒
電極接合体の両面にポリテトラフルオロエチレン
で被覆したチタンリード線付のエキスパンデツド
チタン(外径10mm,内径5mm)からなる集電体を
配設し、それ等全体を多孔性ポリテトラフルオロ
エチレン膜で被覆した。
[Example 1] Platinum (4 mg/
cm 2 ) were joined by electroless plating method, with an outer diameter of 10 mm,
Current collectors made of expanded titanium (outer diameter 10 mm, inner diameter 5 mm) with titanium lead wires coated with polytetrafluoroethylene are placed on both sides of the donut-shaped ion exchange resin membrane-catalyst electrode assembly with an inner diameter of 5 mm. The whole was then covered with a porous polytetrafluoroethylene membrane.

このようにして得られた電気化学セル(濃度セ
ンサ)は電極中央部に水の電気分解により発生し
た酸素と水素が混ざり合うことができるように空
間が設けられている。断面構造図を第1図に示
す。
In the electrochemical cell (concentration sensor) thus obtained, a space is provided in the center of the electrode so that oxygen and hydrogen generated by water electrolysis can mix. A cross-sectional structural diagram is shown in Fig. 1.

[実施例 2] 実施例1と同様、パーフルオロカーボンスルホ
ン酸樹脂膜(デユポン製 ナフイオン117)の両
面に白金(4mg/cm2)を無電解メツキ法により接
合した10mm×10mmのイオン樹脂膜−触媒電極接合
体に直径2mmの穿孔を9箇所設け、その両面にポ
リテトラフルオロエチレンで被覆したチタンリー
ド線付のエキスパンデツドチタン(10mm×10mm)
からなる集電体を配設し、それら全体を多孔性ポ
リテトラフルオロエチレン膜で被覆した。
[Example 2] Similar to Example 1, a 10 mm x 10 mm ionic resin membrane-catalyst was prepared by bonding platinum (4 mg/cm 2 ) to both sides of a perfluorocarbon sulfonic acid resin membrane (DuPont Nafion 117) by electroless plating. Expanded titanium (10 mm x 10 mm) with titanium lead wires, with nine holes of 2 mm in diameter made in the electrode assembly and coated on both sides with polytetrafluoroethylene.
A current collector consisting of the following materials was disposed, and the entirety thereof was covered with a porous polytetrafluoroethylene film.

このようにして得られた電気化学セル(濃度セ
ンサ)では、イオン交換樹脂膜−触媒電極接合体
に均一に分布した穿孔によつて、水の電気分解に
より発生した酸素と水素が極めてスムーズに混合
する。断面構造図を第2図に示す。
In the electrochemical cell (concentration sensor) obtained in this way, the evenly distributed perforations in the ion exchange resin membrane-catalyst electrode assembly allow the oxygen and hydrogen generated by water electrolysis to mix extremely smoothly. do. A cross-sectional structural diagram is shown in Fig. 2.

[実施例 3] 実施例1と同様、パーフルオロカーボンスルホ
ン酸樹脂膜(デユポン製 ナフイオン117)の両
面に白金(4mg/cm2)を無電解メツキ法により接
合した直径3mmのイオン交換樹脂膜−触媒電極接
合体の両面にポリテトラフルオロエチレンで被覆
したチタンリード線付のエキスパンデツドチタン
(直径3mmφ)からなる集電体を配設し、両極に
通じる空間を残して全体を多孔性ポリテトラフル
オロエチレン膜で被覆した。このようにして得ら
れた電気化学セル(濃度センサ)は、イオン交換
樹脂膜−触媒電極接合体と多孔性ポリテトラフル
オロエチレン膜との空間において水の電気分解に
より発生した酸素と水素とが混ざり合うことにな
る。断面構造図を第2図に示す。
[Example 3] Similar to Example 1, platinum (4 mg/cm 2 ) was bonded to both sides of a perfluorocarbon sulfonic acid resin membrane (Nafion 117, manufactured by Dupont) by electroless plating to create an ion exchange resin membrane-catalyst with a diameter of 3 mm. A current collector made of expanded titanium (diameter 3 mmφ) with titanium lead wires coated with polytetrafluoroethylene is arranged on both sides of the electrode assembly, and the entire body is made of porous polytetrafluoroethylene, leaving a space leading to both electrodes. Covered with ethylene membrane. In the electrochemical cell (concentration sensor) obtained in this way, oxygen and hydrogen generated by water electrolysis are mixed in the space between the ion exchange resin membrane-catalyst electrode assembly and the porous polytetrafluoroethylene membrane. It will fit. A cross-sectional structural diagram is shown in Fig. 2.

これらの図において、1,1a,1b,1c,
1dはパーフルオロカーボンスルホン酸樹脂から
なるイオン交換樹脂膜、2,2a,2b,2c,
3dは白金からなる陰極、3,3a,3b,3
c,3dは白金からなる陽極、4,4a,4b,
4c,4dはエキスパンデツドチタンからなる陰
極集電体、5,5a,5bはエキスパンデツドチ
タンからなる陽極集電体、6は多孔性ポリテトラ
フルオロエチレン膜からなる撥水性プラスチツク
膜、7は酸素と水素を混合させるための空間ある
いは孔である。
In these figures, 1, 1a, 1b, 1c,
1d is an ion exchange resin membrane made of perfluorocarbon sulfonic acid resin, 2, 2a, 2b, 2c,
3d is a cathode made of platinum, 3, 3a, 3b, 3
c, 3d are anodes made of platinum, 4, 4a, 4b,
4c and 4d are cathode current collectors made of expanded titanium, 5, 5a, and 5b are anode current collectors made of expanded titanium, 6 is a water-repellent plastic film made of porous polytetrafluoroethylene film, and 7 is a water-repellent plastic film made of porous polytetrafluoroethylene film. A space or hole for mixing oxygen and hydrogen.

次に、これらの電気化学セル(濃度センサ)を
各種濃度に調整した硫酸水溶液に浸漬し、陰極
2,2a,2b,2c,2dと陽極3,3a,3
b,3c,3dとの間に3Vの直流定電圧を印加
した際に流れる電流を測定した結果、第4図に示
す硫酸溶液の水蒸気圧と電流の関係および第5図
に示す硫酸溶液の濃度と電流の関係を得た。
Next, these electrochemical cells (concentration sensors) are immersed in sulfuric acid aqueous solutions adjusted to various concentrations, and cathodes 2, 2a, 2b, 2c, 2d and anodes 3, 3a, 3
As a result of measuring the current that flows when a constant DC voltage of 3V is applied between terminals b, 3c, and 3d, the relationship between the water vapor pressure and current of the sulfuric acid solution shown in Figure 4 and the concentration of the sulfuric acid solution shown in Figure 5 are obtained. The relationship between the current and the current was obtained.

また、これら電気化学セル(濃度センサ)を20
mlの20%硫酸水溶液と共に内容積30mlの容器に封
入し、陰極2,2a,2b,2c,2dと陽極
3,3a,3b,3c,3dとの間に3Vの直流
電圧を印加した際に流れる電流、密閉容器の内
圧、硫酸の濃度の経時変化を第6図イ,ロに示
す。
In addition, 20 of these electrochemical cells (concentration sensors)
ml of 20% sulfuric acid aqueous solution in a container with an internal volume of 30 ml, and when a DC voltage of 3 V was applied between the cathodes 2, 2a, 2b, 2c, 2d and the anodes 3, 3a, 3b, 3c, 3d. Figure 6 A and B show the changes over time in the flowing current, the internal pressure of the sealed container, and the concentration of sulfuric acid.

第4図より電気化学セル(濃度センサ)の電流
が水蒸気圧に正比例すること、第5図より硫酸水
溶液の濃度を電気化学セル(濃度センサ)の電流
から知ることができることがわかる。
It can be seen from FIG. 4 that the current of the electrochemical cell (concentration sensor) is directly proportional to the water vapor pressure, and from FIG. 5 it is possible to know the concentration of the sulfuric acid aqueous solution from the current of the electrochemical cell (concentration sensor).

第6図より測定時間の経過に伴なう水溶液の濃
度変化がなく、また、密閉容器内の圧力変化がな
いことから、測定に伴なうガス発生がないことが
確認された。さらに、測定後、水溶液の水量を測
定し、変化がないことも確認して、測定に伴ない
水溶液が消費されることがないこともわかつた。
As can be seen from FIG. 6, there was no change in the concentration of the aqueous solution as the measurement time elapsed, and there was no change in the pressure inside the closed container, so it was confirmed that there was no gas generation associated with the measurement. Furthermore, after the measurement, the amount of water in the aqueous solution was measured and it was confirmed that there was no change, indicating that the aqueous solution was not consumed during the measurement.

また、硫酸水溶液の濃度を変化させた際の電気
化学セル(濃度センサ)の応答速度は約1分と速
く、この電気化学セル(濃度センサ)によつて硫
酸の濃度を連続的に測定することが可能であるこ
とがわかつた。
In addition, the response speed of the electrochemical cell (concentration sensor) when changing the concentration of the sulfuric acid aqueous solution is as fast as approximately 1 minute, and the concentration of sulfuric acid can be continuously measured using this electrochemical cell (concentration sensor). It turns out that it is possible.

発明の効果 以上述べたように、本発明によれば極めて小さ
な電気化学セル(濃度センサ)に直流の定電圧を
印加し、その電流を測定するだけの簡単な操作で
対象となる水溶液を消費することなく、また、そ
の濃度を変化させることもなく、さらにガスの発
生を伴なわないので、たとえ密閉容器中において
も安全で連続的に水溶液の溶質の濃度を測定する
ことが可能となる。従つて、例えば密閉鉛蓄電池
の硫酸濃度等を測定するのに大きな効果を示し、
その工業的価値は極めて高い。
Effects of the Invention As described above, according to the present invention, a target aqueous solution can be consumed with a simple operation of applying a constant DC voltage to an extremely small electrochemical cell (concentration sensor) and measuring the current. Since the method does not change the concentration or generate gas, it is possible to safely and continuously measure the concentration of the solute in an aqueous solution even in a closed container. Therefore, it is highly effective in measuring the sulfuric acid concentration in sealed lead-acid batteries, for example.
Its industrial value is extremely high.

【図面の簡単な説明】[Brief explanation of the drawing]

第1〜3図は本発明方法を適用した電気化学セ
ルのいくつかの実施例を示す断面構造図、第4図
は硫酸水溶液の水蒸気圧と電気化学セルに流れる
電流との関係を示す図、第5図は硫酸水溶液の濃
度と電気化学セルに流れる電流との関係を示す
図、第6図イ,ロは電気化学セルに流れる電流、
水溶液の濃度および密閉容器の内圧の経時変化を
示す図である。 1,1a,1b,1c,1d……イオン交換樹
脂膜、2,2a,2b,2c,2d……陰極、
3,3a,3b,3c,3d……陽極、6……撥
水性プラスチツク膜。
1 to 3 are cross-sectional structural diagrams showing some examples of electrochemical cells to which the method of the present invention is applied; FIG. 4 is a diagram showing the relationship between the water vapor pressure of an aqueous sulfuric acid solution and the current flowing through the electrochemical cell; Figure 5 is a diagram showing the relationship between the concentration of sulfuric acid aqueous solution and the current flowing through the electrochemical cell, Figure 6 A and B are the current flowing through the electrochemical cell,
FIG. 3 is a diagram showing changes over time in the concentration of an aqueous solution and the internal pressure of a closed container. 1, 1a, 1b, 1c, 1d... ion exchange resin membrane, 2, 2a, 2b, 2c, 2d... cathode,
3, 3a, 3b, 3c, 3d... Anode, 6... Water repellent plastic film.

Claims (1)

【特許請求の範囲】[Claims] 1 イオン交換樹脂膜に陰極および陽極を一体に
接合又は圧接してなる接合体又は圧接体を撥水性
プラスチツク膜で被覆してなる電気化学セルを被
測定水溶液中に浸漬し、陰極と陽極との間に直流
の定電圧を印加した際、前記イオン交換樹脂膜に
吸収される水の電気分解に伴なつて流れる電流が
前記水溶液の溶質の濃度に対応する水蒸気圧に実
質的に正比例する関係を利用して水溶液中の溶質
の濃度を測定する方法において、上記水の電気分
解に伴なつて発生する水素と酸素を混合し、陰・
陽極のいずれか一方あるいは両方の電極表面上で
電極の触媒作用を利用して水に戻すことを特徴と
する水溶液中の溶質の濃度を測定する方法。
1. An electrochemical cell consisting of a bonded body or pressure-bonded body formed by integrally bonding or press-bonding a cathode and an anode to an ion-exchange resin membrane and covering the body with a water-repellent plastic membrane is immersed in an aqueous solution to be measured, and the contact between the cathode and the anode is When a constant DC voltage is applied between them, the current flowing as a result of electrolysis of the water absorbed in the ion exchange resin membrane is substantially directly proportional to the water vapor pressure corresponding to the concentration of the solute in the aqueous solution. In the method of measuring the concentration of solutes in an aqueous solution, hydrogen and oxygen generated during the electrolysis of water are mixed, and an anionic and
A method for measuring the concentration of a solute in an aqueous solution, which is characterized in that the concentration of a solute in an aqueous solution is returned to water using the catalytic action of the electrode on the surface of one or both of the anodes.
JP62026975A 1987-02-06 1987-02-06 Method for measuring concentration of solute in aqueous solution Granted JPS63195558A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62026975A JPS63195558A (en) 1987-02-06 1987-02-06 Method for measuring concentration of solute in aqueous solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62026975A JPS63195558A (en) 1987-02-06 1987-02-06 Method for measuring concentration of solute in aqueous solution

Publications (2)

Publication Number Publication Date
JPS63195558A JPS63195558A (en) 1988-08-12
JPH0534623B2 true JPH0534623B2 (en) 1993-05-24

Family

ID=12208160

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62026975A Granted JPS63195558A (en) 1987-02-06 1987-02-06 Method for measuring concentration of solute in aqueous solution

Country Status (1)

Country Link
JP (1) JPS63195558A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4158654B2 (en) 2003-08-28 2008-10-01 株式会社ジェイテクト Electric power steering device

Also Published As

Publication number Publication date
JPS63195558A (en) 1988-08-12

Similar Documents

Publication Publication Date Title
US5258241A (en) Rebalance cell for a Cr/Fe redox storage system
EP0068508A2 (en) Methanol fuel cell
JPH0374468B2 (en)
JP3025473B2 (en) Electrolytic ozone generator and method for making it
Holze et al. The kinetics of oxygen reduction at Porous Teflon‐Bonded fuel cell electrodes
Liua et al. Partial oxidation of methanol on a metallized Nafion polymer electrolyte membrane
Savinell et al. Discharge Characteristics of a Soluble Iron‐Titanium Battery System
TW542912B (en) Acid gas measuring sensors and method of making same
Kimble et al. A mathematical model of a hydrogen/oxygen alkaline fuel cell
JPH04229960A (en) Gas-recycle battery for electoro- chemical system
Tatapudi et al. Synthesis of hydrogen peroxide in a proton exchange membrane electrochemical reactor
Merkulova et al. Reactions of hydrogen peroxide on a silver electrode in alkaline solution
US5035869A (en) Process for reducing uranyl salt
JPH0640092B2 (en) Humidity measurement method
JPH0534623B2 (en)
JPH027399B2 (en)
US20230010889A1 (en) Device for producing hydrogen and/or ammonia and a method for producing hydrogen and/or ammonia
JPH0569381B2 (en)
Enea Morphological and electrocatalytic properties of gold deposits on NaY zeolite
Alcaide et al. An Impedance Study of the O 2| HO 2− System in Equilibrium on a Gas Diffusion Electrode
JPH0533746B2 (en)
US3894887A (en) Hydrogen-bromine secondary battery
Chen et al. The use of a porous hydrogen diffusion anode in the electrochemical reduction of glucose to sorbitol
JP7713685B2 (en) Hydrogen and/or ammonia production apparatus and method
Michas et al. Metal and metal oxides based membrane composites for solid polymer electrolyte water electrolysers