JPS58618B2 - Method for determining corrosion rate of metals - Google Patents
Method for determining corrosion rate of metalsInfo
- Publication number
- JPS58618B2 JPS58618B2 JP4262277A JP4262277A JPS58618B2 JP S58618 B2 JPS58618 B2 JP S58618B2 JP 4262277 A JP4262277 A JP 4262277A JP 4262277 A JP4262277 A JP 4262277A JP S58618 B2 JPS58618 B2 JP S58618B2
- Authority
- JP
- Japan
- Prior art keywords
- sample metal
- potential
- sample
- metal piece
- corrosion rate
- 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
Landscapes
- Testing Resistance To Weather, Investigating Materials By Mechanical Methods (AREA)
Description
【発明の詳細な説明】
本発明は同じ材質の二つの金属試料片を作用電極とし、
その分極特性を測定することにより所定条件での金属試
料片の腐食速度を判定する方法に関する。[Detailed description of the invention] The present invention uses two metal sample pieces of the same material as working electrodes,
This invention relates to a method for determining the corrosion rate of a metal specimen under predetermined conditions by measuring its polarization characteristics.
金属の腐食速度を測定乃至判定する方法として試料金属
片の分極抵抗RPから求める電気化学的方法が知られて
いる。As a method for measuring or determining the corrosion rate of metal, an electrochemical method is known in which the corrosion rate is determined from the polarization resistance RP of a sample metal piece.
この方法は金属の腐食現象が金属表面から金属イオンを
溶出する一種の電極反応であり、この電極反応速度がそ
のとき流れる電流の大きさに依存することに着目したも
のである。This method focuses on the fact that metal corrosion is a type of electrode reaction that elutes metal ions from the metal surface, and the rate of this electrode reaction depends on the magnitude of the current flowing at that time.
即ち金属試料片を腐食系例えば腐食性溶液中に浸漬した
場合、その金属試料片は一定の腐食電位を示すが、対極
を介して微少の一定電流■を前記試料金属片に与えると
電位変化を起す。That is, when a metal sample piece is immersed in a corrosive system, for example, a corrosive solution, the metal sample piece exhibits a constant corrosion potential, but when a small constant current is applied to the sample metal piece through the counter electrode, the potential changes. cause.
しかしてこの電位変化量をηとすれば試料金属片の分極
抵抗RPは
RP=η/■・・・・・・・・・(1)
で与えられる。However, if the amount of potential change is η, then the polarization resistance RP of the sample metal piece is given by RP=η/■ (1).
一方、理論的には、分極抵抗Rpは次式の如く腐食電流
Icorrと反比例の関係にあると考えられている。On the other hand, theoretically, it is believed that the polarization resistance Rp is inversely proportional to the corrosion current Icorr as shown in the following equation.
RpIcorr=K・・・・・・(2)
ここに、Kは定数で腐食反応について固有な値であり、
実際には腐食電流Icorrの変化に較べ反応の種類に
依存するKの差異は小さい。RpIcorr=K...(2) Here, K is a constant and a value unique to the corrosion reaction,
Actually, the difference in K depending on the type of reaction is small compared to the change in corrosion current Icorr.
また腐食速度Vは次式
%式%(3)
(Mは試料金属の原子量、Zは溶出金属イオンの原子価
数、Fはファラデ一定数)
で示される。Further, the corrosion rate V is expressed by the following formula % (3) (M is the atomic weight of the sample metal, Z is the valence number of the eluted metal ion, and F is the Faraday constant).
従って、(1)式から分極抵抗RPを求めこれを(2)
式に代入して腐食電流Icorrが解れば腐食速度■を
算出しうることになる。Therefore, find the polarization resistance RP from equation (1) and convert it to (2)
If the corrosion current Icorr is known by substituting it into the equation, the corrosion rate ■ can be calculated.
しかしながら上記一定電流を与えた場合の電位変化から
Rpを求め、これから試料金属片の腐食速度を求める方
法においては次のような不都合な問題がある。However, the method of determining Rp from the potential change when a constant current is applied and determining the corrosion rate of the sample metal piece from this method has the following disadvantages.
先ず第一に試料金属片の電位変化量ηが一定値に達する
のに比較的長い時間を要することである。First of all, it takes a relatively long time for the potential change η of the sample metal piece to reach a constant value.
ここで長時間を要することは試料金属片の表面状態の変
化乃至表面へ腐食生成物の堆積を促がし電位変化量η測
定の不正確さを招き易いということになる。If a long time is required here, the change in the surface condition of the sample metal piece or the accumulation of corrosion products on the surface is promoted, which tends to lead to inaccurate measurement of the potential change η.
第二には試料金属片と参照電極との間の溶液抵抗により
生ずる電位降下の影響で試料金属片の電位を正確に測定
し難いことである。Second, it is difficult to accurately measure the potential of the sample metal piece due to the potential drop caused by the solution resistance between the sample metal piece and the reference electrode.
この電位降下は電位変化量ηの変化を追跡する上で大き
な障害となり、また電位降下の影響を補償するには煩雑
な操作を要するという不都合さがある。This potential drop becomes a major hindrance in tracking changes in the amount of potential change η, and there is also the inconvenience that compensating for the influence of the potential drop requires complicated operations.
従って本発明は比較的短かい測定時間内に、腐食電位E
corrが成る程度不安定な系においてもその影響をほ
とんど受けず、また電圧降下の補正乃至補償を要せず容
易に金属の腐食速度を判定(測定)しうる方法を提供し
ようとするものである。Therefore, the present invention can measure the corrosion potential E within a relatively short measurement time.
The purpose of the present invention is to provide a method that is hardly affected by corr even in an unstable system to the extent that corr exists, and that can easily determine (measure) the corrosion rate of metal without requiring correction or compensation for voltage drop. .
以下本発明の詳細な説明すると、本発明は腐食系におか
れた同一材質の二つの試料金属片に一定量の電荷を、一
方をアノード、他方をカソードとして瞬間的に与え、前
記電荷付与による試料金属片間の電位差δの変化を電位
差δ一時間tの関係として開回路状態で測定し、この電
位差δ一時間tの関係を解析して試料金属片の腐食速度
を求めることを特徴とするクーロスタット法を応用した
金属の腐食速度判定法である。To explain the present invention in detail below, the present invention instantaneously applies a certain amount of electric charge to two sample metal pieces of the same material placed in a corrosive system, one as an anode and the other as a cathode. The method is characterized in that the change in the potential difference δ between the sample metal pieces is measured in an open circuit state as a relationship between the potential difference δ and time t, and the corrosion rate of the sample metal piece is determined by analyzing the relationship between the potential difference δ and time t. This is a metal corrosion rate determination method that applies the coulostat method.
第1図は同一材質の二つの試料金属片を、一方をアノー
ド、他方をカソードとしてクーロスタット法を用いて分
極抵抗Rpを測定する原理を説明する回路図で、1は一
定の電気量パルスを発生するパルス発生器を、2はアノ
ードとしての試料金属片を、3はカソードとしての試料
金属片を、4は電位差記録計をそれぞれ示す。Figure 1 is a circuit diagram explaining the principle of measuring the polarization resistance Rp of two metal samples made of the same material using the coulostat method with one as an anode and the other as a cathode. 2 indicates a pulse generator for generating pulses, 2 indicates a sample metal piece as an anode, 3 indicates a sample metal piece as a cathode, and 4 indicates a potentiometer.
しかして第1図の回路を用いて試料金属片の分極抵抗R
Pを求める場合は、所定の腐食電位Ecorr (自然
電位Ecorr)にある二つの試料金属片2,3間に例
えば数μS〜数μ数枚数枚m程度定電気量パルス(電荷
)を与え、二つの試料金属片2,3の電気二重層を瞬間
的に充電する。Using the circuit shown in Figure 1, we can calculate the polarization resistance R of the sample metal piece.
To obtain P, apply a constant electrical pulse (charge) of, for example, several microseconds to several micrometers between two sample metal pieces 2 and 3 that are at a predetermined corrosion potential Ecorr (natural potential Ecorr). The electric double layer of two sample metal pieces 2 and 3 is charged instantaneously.
この場合与える電荷の大きさは試料金属片の電位が腐食
電位Ecorrより数mV程度変化するように選ぶのが
好ましい。In this case, the magnitude of the applied charge is preferably selected so that the potential of the sample metal piece changes by several mV from the corrosion potential Ecorr.
また、二重層充電直前までは両試料金属片間の不斉電位
をなくすために両試料金属片は短絡しておくのが望まし
い。Further, it is desirable that both sample metal pieces be short-circuited until immediately before double layer charging in order to eliminate an asymmetric potential between the two sample metal pieces.
かくして瞬間的に付与された一定量の電荷は腐食反応に
よってアノードおよびカソードとしての両試料金属片2
,3の近傍で消費され、試料金属片の電位は元の状態で
ある腐食電位(自然電位) Ecorrに戻る傾向を示
すのでその電位差δの時間tに対する変化を電位差δ一
時間tの関係として電位差記録計4で記録する。In this way, a certain amount of electric charge instantaneously applied is applied to both the sample metal piece 2 as an anode and a cathode by a corrosion reaction.
, 3, and the potential of the sample metal piece shows a tendency to return to its original corrosion potential (natural potential) Ecorr. Therefore, the change in potential difference δ with respect to time t can be expressed as the potential difference δ - time t relationship. Record with recorder 4.
尚電位差記録計4として入力インピーダンスの大きいも
のを用いる限り両試料金属片2と3との間の電流は無視
でき開回路状態での測定が可能となる。As long as the potentiometer 4 has a large input impedance, the current between the two sample metal pieces 2 and 3 can be ignored and measurement can be performed in an open circuit state.
しかして数mV程程度電位範囲内における試料金属片の
電気二重層の微分容量CDの変化を無視すれば、電位差
δが十分に小さいときは分極値ηも十分に小さくアノー
ド反応またはカソード反応によるファラデー電流■との
間には
RP=η/■
の関係が近似的に成り立つため、アノードとしての試料
金属片またはカソードとしての試料金属片における分極
値η一時間を曲線は一般的には理論的に次のように導か
れる。However, if we ignore the change in the differential capacitance CD of the electric double layer of the sample metal piece within a potential range of about several mV, when the potential difference δ is sufficiently small, the polarization value η is also sufficiently small and the faraday due to the anodic or cathodic reaction Since the relationship RP=η/■ approximately holds true between the current ■ and the polarization value η of the sample metal piece as an anode or the sample metal piece as a cathode, the curve for one hour is generally calculated theoretically. It is derived as follows.
η=η0exp(t/CDRP)
(式中η0は試料金属片に電荷を与えた直後の分極値で
ある。η=η0exp(t/CDRP) (In the formula, η0 is the polarization value immediately after applying an electric charge to the sample metal piece.
)ところで、初期の二重層充電の際にアノードとして用
いた試料金属片にΔQの電荷を与えたとすれば、カソー
ドとして用いた試料金属片には必然的に一ΔQの電荷を
与えたこととなるが、両者の表面積をそれぞれ、Sa、
Scとすれば、アノードとして用いた試料金属片、カソ
ードとして用いた試料金属片の二重層充電直後の分極値
η0a、η0Cはそれぞれ次の如くなる。) By the way, if a charge of ΔQ was given to the sample metal piece used as an anode during the initial double layer charging, a charge of 1 ΔQ was inevitably given to the sample metal piece used as a cathode. However, the surface area of both is Sa,
If Sc, the polarization values η0a and η0C of the sample metal piece used as an anode and the sample metal piece used as a cathode immediately after double layer charging are as follows, respectively.
η0a=ΔQ/Sa・CD・η0c=−ΔQ/SC・C
Dなお、電位差δが十分に小さい場合はCDを一定とみ
なすことができ、CDは自然電位でとる値と同一の値を
とるものとする。η0a=ΔQ/Sa・CD・η0c=−ΔQ/SC・C
D Note that if the potential difference δ is sufficiently small, CD can be considered constant, and CD takes the same value as the natural potential.
したがって、アノードとして用いた試料金属片、カソー
ドとして用いた試料金属片の時間tにおける分極値ηa
、ηcはそれぞれ
η3−η0aexp(−t/CDRP)
=(ΔQ/Sa・CD)exp(−1/CDRP)ηc
=η0cexp(−t/CDRp)
=−(ΔQ/SC・CD)exp(−t/CDRp)の
如く導かれる。Therefore, the polarization value ηa at time t of the sample metal piece used as an anode and the sample metal piece used as a cathode
, ηc are respectively η3-η0aexp(-t/CDRP) = (ΔQ/Sa・CD)exp(-1/CDRP)ηc
It is derived as follows: =η0cexp(-t/CDRp) =-(ΔQ/SC·CD)exp(-t/CDRp).
故に時間tにおける試料金属片間の電位差δは時間の関
数として
の如く、さらに
として導かれる。Therefore, the potential difference δ between the sample metal pieces at time t is further derived as a function of time.
従って電位差δを求めlnδを時間tに対してプロット
したときに直線が得られれば、その直線を時間t=0に
外そうすることによりΔQ/CD(1/Sa+1/Sc
)を求め得る。Therefore, if a straight line is obtained when the potential difference δ is calculated and lnδ is plotted against time t, by removing the straight line at time t=0, ΔQ/CD(1/Sa+1/Sc
) can be obtained.
ここに、ΔQ/CD(1/Sa+1/SC)は二重層充
電直後、時間t=0におけるアノード、カソード間の電
位差δ0に相当する。Here, ΔQ/CD (1/Sa+1/SC) corresponds to the potential difference δ0 between the anode and cathode at time t=0 immediately after double layer charging.
しかして、試料金属片に電荷を与えた直後の分極値δ0
と試料金属片に与えた電荷の量ΔQとから次式
%式%)
によって微分容量CDを求め、さらに、これらのδ0お
よびCDの値を用いれば上記lnδ−を曲線の傾きから
分極抵抗RPを求めうる。Therefore, the polarization value δ0 immediately after applying a charge to the sample metal piece is
Calculate the differential capacitance CD from the following formula and the amount of charge ΔQ given to the sample metal piece.Furthermore, using these values of δ0 and CD, the polarization resistance RP can be calculated from the slope of the curve using the above lnδ−. It can be sought.
次に本発明の実施例を記載する。Next, examples of the present invention will be described.
第2図は二つの試料金属片の電位差変化測定装置である
。FIG. 2 shows an apparatus for measuring changes in potential difference between two sample metal pieces.
これは、腐食測定用セル11中に設置された二つの同一
の材質の試料金属片12,13間に既知量の電荷を与え
る系Aと、前記の両試料金属片12,13間の電位差変
化を追跡する系Bさからなる。This is a system A that applies a known amount of charge between two sample metal pieces 12 and 13 made of the same material installed in the corrosion measurement cell 11, and a change in potential difference between the two sample metal pieces 12 and 13. It consists of a system B that tracks .
既知量の電荷を与える系Aは電荷を供給するための電源
14、上記電荷を予め蓄えておくコンデンサー151〜
154、このコンデンサー151〜154に蓄える電気
量を規制する可変抵抗VR16および上記コンデンサー
151〜154に蓄えられた電荷をセル11の両試料金
属片12゜13の間に瞬間的に与えるリレー17で構成
されている。A system A that provides a known amount of charge includes a power source 14 for supplying the charge, and a capacitor 151 to store the above-mentioned charge in advance.
154, consisting of a variable resistor VR16 that regulates the amount of electricity stored in the capacitors 151 to 154, and a relay 17 that instantaneously provides the charge stored in the capacitors 151 to 154 between both sample metal pieces 12 and 13 of the cell 11. has been done.
なお、リレー17は2回路2接点のものではじめは不斉
電位を無視できるようにするため、試料金属片どうしを
短絡しておき、この試料金属片の短絡解消後、すみやか
に既知量の電荷を与えるような用い方をしている。Note that the relay 17 has two circuits and two contacts, so in order to be able to ignore the asymmetric potential at first, the sample metal pieces are short-circuited together, and after the short-circuit between the sample metal pieces is removed, a known amount of charge is immediately applied to the relay 17. It is used in a way that gives
他方、両試料金属片12,13間の電位差変化を追跡す
る系Bは腐食速度測定用セル11内の両試料金属片12
,13からの信号のインピーダンスを変換する演算増幅
器18および電位差記録計19などから構成されている
。On the other hand, the system B that tracks the potential difference change between the two sample metal pieces 12 and 13 is connected to the two sample metal pieces 12 in the corrosion rate measurement cell 11.
, 13, an operational amplifier 18, a potentiometer 19, and the like.
尚上記電位変化を追跡する系Bにおいて電源20と可変
抵抗21とはポテンシオメータ−を構成しており、この
ポテンシオメータ−は出力信号に一定のバイアスを加え
るためのものである。In the system B for tracking potential changes, the power supply 20 and the variable resistor 21 constitute a potentiometer, and this potentiometer is for applying a constant bias to the output signal.
また前記既知量の電荷を与える系Aのコンデンサー15
1〜154の両端にはそのコンデンサー151〜154
の電圧をチェックしうるようスイッチ22を介して電圧
計23を接続するとともにコンデンサー151〜154
については適当な容量のものを選べるようにロークリ−
スイッチ24が設けである。Also, the capacitor 15 of system A that provides the known amount of charge.
The capacitors 151 to 154 are connected to both ends of 1 to 154.
A voltmeter 23 is connected via the switch 22 to check the voltage of the capacitors 151 to 154.
As for
A switch 24 is provided.
上記の如く構成された電位差変化測定装置において試料
金属片12および13として、それぞれ1cm2.1.
5cm2の表面積を有する純銅板を用いセル11中に市
水を収容した状態で、先ずその銅板の腐食電位(自然電
位)を参照電極として5CE(飽和せコウ電極)を用い
て求めたところ−0,230Vvs、SCEであった。In the potential difference measurement device configured as described above, the sample metal pieces 12 and 13 are each 1 cm2.1.
Using a pure copper plate with a surface area of 5 cm2 and with city water contained in the cell 11, the corrosion potential (natural potential) of the copper plate was first determined using a 5CE (saturated corrosion electrode) as a reference electrode. , 230V vs. SCE.
次いで両試料金属片12,13にそれぞれ、+0.14
3μC2−0,143μCの電荷を瞬時与えたところ電
位差δと時間tとの関係は第3図に示す如くであった。Next, +0.14 was applied to both sample metal pieces 12 and 13, respectively.
When a charge of 3 .mu.C2-0.143 .mu.C was applied instantaneously, the relationship between the potential difference .delta. and the time t was as shown in FIG.
第3図示のδ−を曲線において電位差δの対数logδ
として表示したところ時間tとの関係は第4図の如く直
線関係があり、logδをt=0に外挿すると試料金属
片に電荷を与えた直後の電位差δ0=6.8mVが得ら
れ、また
の式からCD=35μF/cm2が、さらに第4図示の
直線の傾きから分極抵抗RP=213にΩが得られた。The logarithm logδ of the potential difference δ is calculated using the curve δ− shown in Figure 3.
When expressed as , there is a linear relationship with time t as shown in Figure 4, and if log δ is extrapolated to t = 0, a potential difference δ0 = 6.8 mV immediately after applying a charge to the sample metal piece is obtained, and From the equation, CD=35 μF/cm2, and from the slope of the straight line shown in FIG. 4, polarization resistance RP=213Ω was obtained.
この分極抵抗RP=213にΩの値は定電流法で求めた
値215にΩとほぼ一致していた。The value of Ω for this polarization resistance RP=213 was approximately equal to the value 215 Ω determined by the constant current method.
上記各個を(2)、(3)式によって腐食速度■に換算
すると0.27mdd、0.26mddとなり浸漬法に
よる測定値0.266mddとほぼ一致していた。When each of the above values was converted into a corrosion rate (■) using equations (2) and (3), the results were 0.27 mdd and 0.26 mdd, which were almost in agreement with the value measured by the immersion method, which was 0.266 mdd.
尚上記において腐食系に抵抗の大きい市水を用いても、
浸漬法による場合とほぼ一致した値が得られるのは電位
降下を考慮しての補正を無視し得ることを意味する。In addition, even if city water with high resistance to corrosive systems is used in the above,
The fact that values almost identical to those obtained by the immersion method can be obtained means that corrections taking into account the potential drop can be ignored.
上記の如く本発明方法によれば電位降下を考慮した補正
が不要となり、測定上の煩雑さを省けるばかりでなく測
定精度も向上し得る。As described above, according to the method of the present invention, there is no need for correction in consideration of potential drop, which not only eliminates the complexity of measurement but also improves measurement accuracy.
さらに定電流法による腐食速度の判定乃至測定に較べ短
時間内に行ないうる。Furthermore, the corrosion rate can be determined or measured in a shorter time than the constant current method.
例えばステンレス鋼の腐食速度判定を定電流法で行なっ
た場合は、二重層の充電に長時間要し、結局一定の分極
値に達するのに相当時間がかかり測定時間として数10
分〜数時間も要するのに対して本発明方法による場合は
数秒程度で著しく短時間内に行ないうる。For example, when determining the corrosion rate of stainless steel using the constant current method, it takes a long time to charge the double layer, and it takes a considerable amount of time to reach a certain polarization value, resulting in a measurement time of several tens of thousands of hours.
The method of the present invention can be carried out in an extremely short time, on the order of several seconds, whereas the method of the present invention requires several minutes to several hours.
従って本発明方法によれば、試料金属片(作用電極)の
表面状態や腐食系の変化に伴ない試料金属片の自然電位
が不安定性を示し易い場合でも判定できることになる。Therefore, according to the method of the present invention, determination can be made even when the natural potential of the sample metal piece (working electrode) tends to show instability due to changes in the surface condition of the sample metal piece (working electrode) or the corrosion system.
しかも、本発明は同じ材質の試料金属片をアノードおよ
びカソードとして用いる2電極法によるクーロスタット
法を利用しているので、操作が簡単で、それだけ浸食速
度の判定も迅速に行なうことができる。Furthermore, since the present invention utilizes a two-electrode coulostat method in which a sample metal piece of the same material is used as an anode and a cathode, the operation is simple and the erosion rate can be determined quickly.
第1図はクーロスタット法により試料金属片の分極抵抗
を求める原理の説明図、第2図は本発明の一実施例に用
いた電位差変化測定装置の回路図、第3図および第4図
は上記実施例において求めた電位差と時間との関係をそ
れぞれ示す関係図である。
11・・・・・・腐食速度測定用セル、12,13・・
・・・・試料金属片、14・・・・・・電源、151〜
154・・・・・・コンデンサ、16・・・・・・可変
抵抗、17・・・・・・リレー、18・・・・・・演算
増幅器、19・・・・・・電位差記録計、20・・・・
・・電源、21・・・・・・可変抵抗。Fig. 1 is an explanatory diagram of the principle of determining the polarization resistance of a sample metal piece by the coulostat method, Fig. 2 is a circuit diagram of a potential difference change measuring device used in an embodiment of the present invention, and Figs. 3 and 4 are FIG. 6 is a relationship diagram showing the relationship between the potential difference and time determined in the above example. 11... Corrosion rate measurement cell, 12, 13...
...Sample metal piece, 14...Power supply, 151~
154... Capacitor, 16... Variable resistor, 17... Relay, 18... Operational amplifier, 19... Potentiometer, 20・・・・・・
...Power supply, 21...Variable resistance.
Claims (1)
一方をアノード、他方をカソードとして所定量の電荷を
瞬間的に与え、前記両試料金属片間の電位差δの変化を
電位差δ一時間tの関係として開回路状態で測定し、こ
の測定結果から前記試料金属片の腐食速度を求めること
を特徴とする金属の腐食速度判定法。1 Two sample metal pieces of the same material placed in a corrosive system,
A predetermined amount of charge is instantaneously applied to one of the metal pieces as an anode and the other as a cathode, and the change in the potential difference δ between the two sample metal pieces is measured in an open circuit state as a relationship between the potential difference δ and time t. A metal corrosion rate determination method characterized by determining the corrosion rate of a sample metal piece.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4262277A JPS58618B2 (en) | 1977-04-15 | 1977-04-15 | Method for determining corrosion rate of metals |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4262277A JPS58618B2 (en) | 1977-04-15 | 1977-04-15 | Method for determining corrosion rate of metals |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS53128384A JPS53128384A (en) | 1978-11-09 |
| JPS58618B2 true JPS58618B2 (en) | 1983-01-07 |
Family
ID=12641109
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4262277A Expired JPS58618B2 (en) | 1977-04-15 | 1977-04-15 | Method for determining corrosion rate of metals |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58618B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018074231A1 (en) | 2016-10-20 | 2018-04-26 | 東ソー・ファインケム株式会社 | Aluminum alloy-containing composition, production method therefor, and trialkyl aluminum production method |
-
1977
- 1977-04-15 JP JP4262277A patent/JPS58618B2/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018074231A1 (en) | 2016-10-20 | 2018-04-26 | 東ソー・ファインケム株式会社 | Aluminum alloy-containing composition, production method therefor, and trialkyl aluminum production method |
| KR20190072575A (en) | 2016-10-20 | 2019-06-25 | 토소 화인켐 가부시키가이샤 | COMPOSITION CONTAINING ALUMINUM ALLOY, METHOD FOR PRODUCING THE SAME, AND METHOD FOR PRODUCING TRIACEL ALUMINUM |
| EP3822279A1 (en) | 2016-10-20 | 2021-05-19 | Tosoh Finechem Corporation | Method for producing trialkylaluminum |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS53128384A (en) | 1978-11-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5180968A (en) | Method and apparatus for compensation of double layer charging current in electrochemical cells | |
| US3969667A (en) | Device for determining the state of charge in batteries | |
| US3868578A (en) | Method and apparatus for electroanalysis | |
| US4056445A (en) | Determination of corrosion rates by an electrochemical method | |
| US4130464A (en) | Method of evaluating the corrosion rates of metals | |
| JPS5926660B2 (en) | Measuring method of electroless plating reaction | |
| US4119909A (en) | Pulsed DC transient conductivity measurement system | |
| CN102590294B (en) | Automatic measurement and compensation method for uncompensated resistance of electrochemical system | |
| Andrieux et al. | Ultramicroelectrodes for fast electrochemical kinetics | |
| GB1580229A (en) | Method and means for determining the immersed surface area of an electrode of an electrochemical bath | |
| Van Leeuwen | The coulostatic impulse technique: a critical review of its features and possibilities | |
| US3717566A (en) | Corrosion ratemeter | |
| JPH071289B2 (en) | Method and apparatus for measuring conductivity without influence of polarization | |
| JPS58618B2 (en) | Method for determining corrosion rate of metals | |
| Williams et al. | iR correction: Part I. A computerised interrupt method | |
| JPS5822697B2 (en) | Method for measuring rate factors of corrosion reactions | |
| EP0597475A1 (en) | Method of monitoring major constituents in plating baths containing codepositing constituents | |
| US2886770A (en) | Polarographic method and apparatus | |
| JP3051153B2 (en) | Under-film corrosion measuring device | |
| RU2135987C1 (en) | Coulometric plant with controlled potential | |
| Willihnganz | Resistance and polarization in a storage battery | |
| Kooijman | A new analysis of data obtained with galvanostatic and coulostatic single pulses | |
| JPS5926663B2 (en) | Electroless plating reaction measuring device | |
| US2842736A (en) | Polarograph | |
| RU2103676C1 (en) | Method of compensation of series active resistance of electrochemical cell in voltammetry |