JPH0612355B2 - Metal surface contamination degree detection method - Google Patents
Metal surface contamination degree detection methodInfo
- Publication number
- JPH0612355B2 JPH0612355B2 JP61153550A JP15355086A JPH0612355B2 JP H0612355 B2 JPH0612355 B2 JP H0612355B2 JP 61153550 A JP61153550 A JP 61153550A JP 15355086 A JP15355086 A JP 15355086A JP H0612355 B2 JPH0612355 B2 JP H0612355B2
- Authority
- JP
- Japan
- Prior art keywords
- metal
- current
- potential
- contamination
- chromic acid
- 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
Links
- 238000011109 contamination Methods 0.000 title claims description 29
- 229910052751 metal Inorganic materials 0.000 title claims description 27
- 239000002184 metal Substances 0.000 title claims description 27
- 238000001514 detection method Methods 0.000 title description 2
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 claims description 27
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 claims description 27
- 239000000243 solution Substances 0.000 claims description 24
- 230000003749 cleanliness Effects 0.000 claims description 10
- 238000005259 measurement Methods 0.000 claims description 8
- 239000008151 electrolyte solution Substances 0.000 claims description 5
- 238000002791 soaking Methods 0.000 claims 1
- 239000000463 material Substances 0.000 description 27
- 229910000881 Cu alloy Inorganic materials 0.000 description 23
- 238000006722 reduction reaction Methods 0.000 description 18
- 238000012360 testing method Methods 0.000 description 18
- 238000000034 method Methods 0.000 description 17
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 16
- 229910052799 carbon Inorganic materials 0.000 description 16
- 230000009467 reduction Effects 0.000 description 14
- 238000004519 manufacturing process Methods 0.000 description 13
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 9
- 229910052802 copper Inorganic materials 0.000 description 9
- 239000010949 copper Substances 0.000 description 9
- 239000000523 sample Substances 0.000 description 9
- 239000003575 carbonaceous material Substances 0.000 description 8
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 6
- 230000010287 polarization Effects 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 239000007769 metal material Substances 0.000 description 5
- 229910052697 platinum Inorganic materials 0.000 description 5
- 230000001603 reducing effect Effects 0.000 description 5
- 239000000956 alloy Substances 0.000 description 4
- 238000000137 annealing Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 230000001590 oxidative effect Effects 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 229910021607 Silver chloride Inorganic materials 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 229910052709 silver Inorganic materials 0.000 description 3
- 239000004332 silver Substances 0.000 description 3
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229920000742 Cotton Polymers 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 2
- 238000013473 artificial intelligence Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005238 degreasing Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000010687 lubricating oil Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229910001361 White metal Inorganic materials 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- GTKRFUAGOKINCA-UHFFFAOYSA-M chlorosilver;silver Chemical compound [Ag].[Ag]Cl GTKRFUAGOKINCA-UHFFFAOYSA-M 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001493 electron microscopy Methods 0.000 description 1
- 238000001941 electron spectroscopy Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000005488 sandblasting Methods 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 239000010969 white metal Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Testing Resistance To Weather, Investigating Materials By Mechanical Methods (AREA)
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は銅または銅合金の製造工程や表面改質(サンド
ブラスト、酸洗等)あるいはカーボン質に起因する銅ま
たは銅合金の表面清浄度、汚染度の判定のための金属表
面の汚染度検出方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to the production process of copper or copper alloy, surface modification (sandblasting, pickling, etc.), or surface cleanliness of copper or copper alloy due to carbonaceous material, The present invention relates to a method for detecting the degree of contamination on a metal surface for determining the degree of contamination.
銅または銅合金材のカーボン質付着に起因する材料表面
の汚染度の判定としては、硝酸液中に金属を浸漬後、表
面を脱脂綿で拭きとり、綿の黒化度で判定する方法が知
られている。しかしながら、この方法は感度が低く、定
量性が無いことから、実用に供されていない。To determine the degree of contamination of the material surface caused by the carbonaceous adhesion of copper or copper alloy material, after immersing the metal in nitric acid solution, wipe the surface with absorbent cotton, and determine the degree of blackening of cotton. ing. However, this method has not been put to practical use because of its low sensitivity and lack of quantitativeness.
ところで、プラントや冷熱機器の熱交換器として多用さ
れる銅または銅合金管材の淡水、海水中の異常腐蝕の一
因として、製造工程に起因する材料表面のカーボン質に
よる汚染が考えられていたが、適当な検出手段が無く、
対策として表面層を一層削る等の対策がとられていた。By the way, as a cause of abnormal corrosion of copper or copper alloy pipes, which is often used as a heat exchanger for plants and cooling equipment, in fresh water and seawater, it was thought that carbon contamination of the material surface due to the manufacturing process was considered. , There is no suitable detection means,
As a countermeasure, some measures such as shaving the surface layer were taken.
しかしながら、この処置が適正であったか否かは検知す
る手段が無かった。However, there was no means to detect whether or not this treatment was appropriate.
すなわち、電子分光、電子顕微鏡、X線分析等はほとん
ど役に立たない。That is, electron spectroscopy, electron microscopy, X-ray analysis and the like are of little use.
そこでこの発明の目的とするところは、簡単な方法によ
って鋭敏にその汚染度を判定することの出来る金属表面
の汚染度検出方法を提供することにある。Therefore, an object of the present invention is to provide a method for detecting the degree of contamination of a metal surface, which can detect the degree of contamination sharply by a simple method.
上記目的を達成するため本発明は次の手法を用いる。す
なわち、被検査金属に対向して対極電極を配し、また、
これらの間に配されて被検査金属との間に電位差を与え
るための基準電極を設けて被検査金属と基準電極との間
に電位差を与えるとともに、これらをクロム酸溶液に浸
し、被検査金属と対極電極との間に流れる電流を計測す
ることにより、被検査金属についてクロム酸溶液をベー
スとした電解液中での電流を計測する計測工程と、前記
計測工程から得られた電流の状態から被検査金属の清浄
度または汚染度を判定する判定工程とを用いる。In order to achieve the above object, the present invention uses the following method. That is, the counter electrode is arranged facing the metal to be inspected,
A reference electrode is provided between these to provide a potential difference between the metal to be inspected and a potential difference is provided between the metal to be inspected and the reference electrode, and these are immersed in a chromic acid solution to remove the metal to be inspected. By measuring the current flowing between the counter electrode and the counter electrode, from the measurement step of measuring the current in the electrolyte based on the chromic acid solution for the metal to be inspected, from the state of the current obtained from the measurement step And a determination step of determining the cleanliness or contamination of the metal to be inspected.
本発明では金属材料素地を痛めずに(腐蝕しない)酸化
作用のあり、カーボン質表面では還元作用の活発な電解
液を用いる。この条件を満たす電解液としては、クロム
酸があり、このクロム酸を用いる。このクロム酸を基本
とした電解液中に被検査金属体を浸漬させ、その溶液中
で金属を分極させ、発生する還元電流の大きさを計測し
て、表面の清浄度または汚染度を判定する。すなわち、 HCrO4 −+7H++3e →Cr++++4H2O なる反応による(Cr6価)→(Cr3価)の還元反応
がカーボン質では活性で、電流が流れ易いことを利用し
て汚染度または洗浄度を検査する。In the present invention, an electrolytic solution that has an oxidizing action without damaging (not corroding) the metal material base and has an active reducing action on the carbonaceous surface is used. Chromic acid is used as an electrolytic solution satisfying this condition, and this chromic acid is used. The metal to be inspected is immersed in this chromic acid-based electrolyte, the metal is polarized in the solution, and the magnitude of the reducing current generated is measured to determine the cleanliness or contamination of the surface. . That is, the reduction reaction of (Cr6 valence) → (Cr3 valence) due to the reaction of HCrO 4 − + 7H + + 3e → Cr +++ + 4H 2 O is active in the carbonaceous material, and the degree of contamination or the degree of cleaning is based on the fact that an electric current easily flows. To inspect.
従って、本発明によれば、簡単な方法によって鋭敏にそ
の汚染度または洗浄度を判定することの出来る金属表面
の汚染度検出方法を提供できる。Therefore, according to the present invention, it is possible to provide a method for detecting the degree of contamination on a metal surface, which can determine the degree of contamination or the degree of cleaning sharply by a simple method.
初めに本発明の原理を説明する。 First, the principle of the present invention will be described.
本発明は金属材料素地を痛めず(腐蝕しない)しかも酸
化作用があり、カーボン質表面(カーボン単体の表面)
では還元作用の活発な溶液であるクロム酸溶液を電解液
として用いる。このクロム酸を基本とした電解液中に被
検査金属体を浸漬させ、その溶液中で金属を分極させ、
+0.6〜0V(銀/塩化銀電極基準)の電位域に発生
する還元電流の大きさを計測して、表面の清浄度または
汚染度を判定する。INDUSTRIAL APPLICABILITY The present invention does not damage the metal base material (does not corrode) and has an oxidizing action, and has a carbonaceous surface (the surface of carbon alone).
Then, a chromic acid solution, which is a solution having a vigorous reducing action, is used as the electrolytic solution. The metal to be inspected is immersed in this chromic acid-based electrolyte, and the metal is polarized in the solution.
The level of reduction current generated in the potential range of +0.6 to 0 V (based on silver / silver chloride electrode) is measured to determine the cleanliness degree or contamination degree of the surface.
すなわち、クロム酸の還元反応の平衡電位は理論上、次
の式で示される。That is, the equilibrium potential of the reduction reaction of chromic acid is theoretically expressed by the following equation.
HCrO4 −+7H++3e →Cr++++4H2O …(1) 銀−塩化銀基準E(in3.3MkCl)は E=1. 144−0. 1379PH+0. 0197・log(〔HCr
O4 −〕/〔Cr+++〕) 還元電位は液のPH(ペーハー)、 〔HCrO4 −〕/〔Cr+++〕の濃度比で変化す
る。HCrO 4 − + 7H + + 3e → Cr +++ + 4H 2 O (1) The silver-silver chloride standard E (in 3.3 MkCl) is E = 1.144-0. 1379PH + 0.0197 · log ([HCr
O 4 − ] / [Cr +++ ]) The reduction potential changes depending on the concentration ratio of PH (pH) and [HCrO 4 − ] / [Cr +++ ] of the liquid.
この平衡電位から電位Exを卑の方向に変化させると、
電位塩化(E−Ex)=△Eに応じて、第1式の3e
(電気量)に相当する電流が流れる。Varying from the equilibrium potential of the potential E x in the direction of the less noble,
Depending on the potential chloride (E−E x ) = ΔE, 3e of the first equation
A current corresponding to (electrical quantity) flows.
しかし、この電流は反応の起こる表面物質で異なり、例
えば、白金単体では電位変化△Eを大きく変化させて
も、電流は流れず、不活性である。これに対し、カーボ
ン単体は第4図に見られるように+0.6Vから電流が
流れ始め、+0.4V付近でピークを生じ、再び電位の
低下とともに電流が低下するように第1式の反応に極め
て活性である。このように、第1式の反応による(Cr
6価)→(Cr3価)の還元反応がカーボン質では活性
で、電流が流れ易い。However, this current is different depending on the surface substance on which the reaction occurs, and, for example, platinum alone is inactive because no current flows even if the potential change ΔE is greatly changed. On the other hand, as shown in FIG. 4, in the simple substance of carbon, the current starts to flow from + 0.6V and a peak occurs at around + 0.4V, and the current decreases with the decrease of the potential. Very active. Thus, the reaction of the first equation (Cr
A reduction reaction of (hexavalent) → (trivalent Cr) is active in carbonaceous matter, and an electric current easily flows.
従って、白金表面にカーボンが付着すれば、上記の電位
条件で電流が流れるので、これより直ちに被検査金属材
の表面の汚れ具合を知ることが出来る。Therefore, if carbon adheres to the platinum surface, a current flows under the above-mentioned potential condition, so that the degree of contamination on the surface of the metal material to be inspected can be immediately known.
クロム酸濃度、ベースとなる材質、カーボンの付着程度
(分布)、温度、電解液の流動の具合によってこの電流
の生じる電位は若干変動するが、+0.6Vから0Vの
範囲の電位における発生電流を用いれば、この各種条件
による違いをほとんどカバーでき、被検査金属材の表面
の汚れ具合を検知することが出来る。The potential generated by this current varies slightly depending on the concentration of chromic acid, the material used as the base, the degree of carbon deposition (distribution), the temperature, and the flow of the electrolyte, but the generated current in the potential range of +0.6 V to 0 V varies. If used, it is possible to cover most of the differences due to these various conditions, and it is possible to detect the degree of dirt on the surface of the inspected metal material.
本発明はこのような原理にに基づくもので、以下その一
実施例について図面を参照して説明する。The present invention is based on such a principle, and one embodiment thereof will be described below with reference to the drawings.
本発明は銅または銅合金の製造工程において生じるカー
ボン質による汚染度の検出方法に関するものであり、ご
みや腐食生成物あるいは油等による汚れは対象外であ
る。The present invention relates to a method for detecting the degree of contamination by carbonaceous substances generated in the manufacturing process of copper or copper alloys, and does not include dirt due to dust, corrosion products, oil or the like.
第1図に本発明にかかる一実施例のフローシィートを示
す。第1図において、1は容器、2はクロム酸溶液、3
は電磁撹拌機、4は撹拌翼を示している。FIG. 1 shows a flow sheet of an embodiment according to the present invention. In FIG. 1, 1 is a container, 2 is a chromic acid solution, 3
Is an electromagnetic stirrer, and 4 is a stirring blade.
容器1内のクロム酸溶液2は電磁撹拌機3と撹拌翼4で
一定条件に撹拌される。このクロム酸溶液2中に供試材
5、白金板等の対極6、供試材5の電極電位を計測する
基準電極7が浸漬されている。The chromic acid solution 2 in the container 1 is agitated by the electromagnetic agitator 3 and the agitating blade 4 under constant conditions. A sample material 5, a counter electrode 6 such as a platinum plate, and a reference electrode 7 for measuring the electrode potential of the sample material 5 are immersed in the chromic acid solution 2.
また、前記供試材5はリード線8aで、前記対極6はリ
ード線8bで、前記基準電極7はリード線8cによって
それぞれポテンショスタット9に結線されている。Further, the test material 5 is connected to the lead wire 8a, the counter electrode 6 is connected to the lead wire 8b, and the reference electrode 7 is connected to the potentiostat 9 by the lead wire 8c.
このような構成において、ポテンショスタット9は供試
材5と基準電極7との間の電位差を第2式に示すよう
に、一定速度で変化させるものである。In such a configuration, the potentiostat 9 changes the potential difference between the sample material 5 and the reference electrode 7 at a constant speed as shown in the second equation.
Et=EN+vt (dE/dt)=v …(2) ここに、ENは供試材5の自然電位、Etは供試材5の
時刻tにおける電位、vは電位走査速度である。Et = E N + vt (dE / dt) = v (2) Here, E N is the natural potential of the sample material 5, Et is the potential of the sample material 5 at time t, and v is the potential scanning speed.
この電位差Etに対応してポテンショスタット9から電
流10がリード線8b,対極6,クロム酸溶液2,供試
材5,リード線8a,ポテンショスタット9を通して流
れ、この際の電流10は供試材5のクロム酸イオンに対
する活性の度合で異なる。A current 10 flows from the potentiostat 9 through the lead wire 8b, the counter electrode 6, the chromic acid solution 2, the test material 5, the lead wire 8a, and the potentiostat 9 in response to this potential difference Et, and the current 10 at this time is the test material. 5 depends on the degree of activity with respect to chromate ion.
第2図は銅合金供試材I(A社製)、第3図は銅合金供
試材II(B社製)、第4図はカーボン材、第5図は白金
材の電位差と電流の計測結果の一例を示した図である。Fig. 2 shows the copper alloy test material I (manufactured by Company A), Fig. 3 shows the copper alloy test material II (manufactured by Company B), Fig. 4 shows the carbon material, and Fig. 5 shows the potential difference and current of the platinum material. It is a figure showing an example of a measurement result.
第2図の銅合金供試材I、第3図の銅合金供試材IIは製
造工程の異なる銅合金材を比較のために示してある。す
なわち、第2図の銅合金供試材Iは汚染が激しく、第3
図の銅合金供試材IIは汚染がない。また、第8図は銅合
金供試材Iと同様の銅合金供試材Iをカーボン汚染を除
去して後の陰分極曲線を示したものである。これを見る
とわかるように第2図に比べ、全体として電流が小さく
なり、高電位域ではフラットな分布となって、明らかに
汚染状態の時と全く異なる曲線を示している。The copper alloy test material I in FIG. 2 and the copper alloy test material II in FIG. 3 show copper alloy materials having different manufacturing steps for comparison. That is, the copper alloy test material I shown in FIG.
The copper alloy test material II in the figure is free of contamination. Further, FIG. 8 shows a negative polarization curve of the copper alloy test material I similar to the copper alloy test material I after removing the carbon contamination. As can be seen, compared to FIG. 2, the current becomes smaller as a whole, and the distribution becomes flat in the high potential region, showing a curve that is completely different from that in the contaminated state.
すなわち、供試材の表面がカーボンなどで汚染されてい
るとクロム酸溶液中で前記第1式に基づく電流が流れる
から、第2図の銅合金供試材Iと第3図の銅合金供試材
IIの差は製造工程の違いによる表面清浄度の違いによる
ものと考えられる。例えば、製造工程が銅管を引き抜き
製作する場合の潤滑油の洗浄の不具合、焼鈍工程におけ
る不活性ガスの純度の不具合等によって、このように管
の表面清浄度に差が出てくる。このような被検査材表面
清浄度の差は従来計測出来なかったが、本発明によれ
ば、上述のようにはっきりとこの清浄度の違いがわかる
ようになる。That is, when the surface of the test material is contaminated with carbon or the like, the electric current based on the above formula 1 flows in the chromic acid solution. Therefore, the copper alloy test material I of FIG. 2 and the copper alloy test material of FIG. Trial material
The difference in II is considered to be due to the difference in surface cleanliness due to the difference in manufacturing process. For example, such a difference in surface cleanliness of the pipe occurs due to a defect in cleaning the lubricating oil when the copper pipe is drawn out in the manufacturing process and a defect in the purity of the inert gas in the annealing process. Conventionally, such a difference in cleanliness of the material to be inspected could not be measured, but according to the present invention, the difference in cleanliness can be clearly recognized as described above.
第2図ないし第5図から明らかなようにカーボン材はク
ロム酸の還元に極めて活発で、電流のピーク値によっ
て、銅合金の表面がカーボン材で汚染されているか否
か、鋭敏に検知できることがわかる。As is clear from FIGS. 2 to 5, the carbon material is extremely active in the reduction of chromic acid, and the peak value of the current makes it possible to detect sensitively whether the surface of the copper alloy is contaminated with the carbon material. Recognize.
第2図ないし第5図の計測条件は以下の通りである。The measurement conditions of FIGS. 2 to 5 are as follows.
.電解液 0.1Mクロム酸溶液 .電位走査速度 125V/min もう少し具体的に説明する。本発明はカーボン質による
汚染度の検出方法に関するものであるが、銅または銅合
金の製造工程において生じるカーボン質による汚染度の
検出に使用する。そして、本発明はカーボン電極が、ク
ロム酸イオンの還元に極めて活性であることを見出し、
この現象を利用してカーボン質が付着した銅あるいは銅
合金材のクロム酸液中での還元電流を求めたところ、還
元電流の大きさと表面の汚染度との間に非常に良い相関
が得られたのでこの事実を利用した。. Electrolyte solution 0.1M chromic acid solution. Potential scanning speed 125 V / min A more specific description will be given. The present invention relates to a method for detecting the degree of contamination by carbonaceous matter, which is used for detecting the degree of contamination caused by carbonaceous matter that occurs in the manufacturing process of copper or copper alloy. And the present invention finds that the carbon electrode is extremely active in the reduction of chromate ions,
Using this phenomenon, we calculated the reduction current of copper or copper alloy material with carbonaceous material in a chromic acid solution, and obtained a very good correlation between the magnitude of the reduction current and the degree of surface contamination. I took advantage of this fact.
本発明においては、還元電流の大きさは以下の手順に従
い測定する。In the present invention, the magnitude of reduction current is measured according to the following procedure.
第1図の構成に示すように、まず容器1内にクロム酸溶
液2を満たす。このクロム酸溶液2中に供試材5、対極
6及び供試材5の電位を測定する基準電極7を浸漬す
る。As shown in the configuration of FIG. 1, first, the container 1 is filled with the chromic acid solution 2. The sample material 5, the counter electrode 6, and the reference electrode 7 for measuring the potentials of the sample material 5 are immersed in the chromic acid solution 2.
このような構成において、ポテンショスタット9を用い
て供試材5の電位を自然電位(溶液中に浸漬した金属が
示す電位)からマイナス方向へ変化させ、そのとき対極
6との間に流れる電流を測定する。この電位と電流の関
係曲線を分極曲線と云い、マイナス方向へ電位を変化さ
せる場合の関係曲線を陰分極曲線と呼ぶ(第2図乃至第
5図)。In such a configuration, the potentiostat 9 is used to change the potential of the sample material 5 from the natural potential (the potential indicated by the metal immersed in the solution) to the negative direction, and at that time, the current flowing between the counter electrode 6 and the counter electrode 6 is changed. taking measurement. The relationship curve between the potential and the current is called a polarization curve, and the relationship curve when the potential is changed in the negative direction is called a negative polarization curve (FIGS. 2 to 5).
第4図のカーボン単体の陰分極曲線において、+0.6
V〜0V(銀/塩化銀基準電極に対して)の電位領域に
おいて、数10mAの還元電流が流れることがわかる。
また、第2図に示すカーボン汚染が激しいA社製銅合金
供試材Iでも、同様に還元電流が流れることがわかる。In the negative polarization curve of carbon alone in FIG. 4, +0.6
It can be seen that a reducing current of several tens of mA flows in the potential region of V to 0 V (with respect to the silver / silver chloride reference electrode).
Further, it can be seen that the reduction current also flows in the copper alloy test material I manufactured by Company A with severe carbon contamination shown in FIG.
これに対して第3図に示すカーボン汚染の無いB社製の
銅合金供試材II及び第5図に示す白金単体では+0.6
V〜0Vの電位領域においての還元電流は1mA以下と
極めて小さい。このため、予めカーボン汚染度と還元電
流の関係を求めておくことにより、測定された還元電流
の大きさよりカーボン質による汚染度を評価することが
できる。On the other hand, the copper alloy test material II manufactured by Company B without carbon pollution shown in FIG. 3 and the platinum simple substance shown in FIG.
The reduction current in the potential region of V to 0 V is extremely small, 1 mA or less. Therefore, by previously obtaining the relationship between the carbon contamination level and the reduction current, it is possible to evaluate the carbon contamination level from the measured reduction current level.
なお、本発明はインピーダンス法を適用することもでき
る。そして、この場合のインピーダンス法は供試材5と
基準電極7との間に交流電圧を印加し、そのとき流れる
交流電流を測定しインピーダンス(電圧/電流)を求め
るものであり、基本的には陰分極曲線測定法と変わらな
い。The impedance method can also be applied to the present invention. The impedance method in this case applies an AC voltage between the sample material 5 and the reference electrode 7, measures the AC current flowing at that time, and obtains the impedance (voltage / current). It is no different from the negative polarization curve measurement method.
つぎに第6図は第2図で示した銅合金供試材Iをサンド
プラスティングしたものであるが、完全にカーボン材が
除去されてないことを示している。Next, FIG. 6 shows that the copper alloy test material I shown in FIG. 2 is sand-plasted, but shows that the carbon material is not completely removed.
表面から、約100μm研削した第8図のものは、第3
図、第5図とほとんど変らず、完全に汚染が除去できた
ことが確認出来る。The one in FIG. 8 ground about 100 μm from the surface is the third
It can be confirmed that the contamination was completely removed, almost the same as in Fig. 5 and Fig. 5.
クロム酸の還元ピーク電流の大きさは、クロム酸濃度、
溶液の撹拌状態、電位走査速度、温度等で異なるので、
これら条件を一定にした計測が再現性、精度の上からも
必要である。一般に、カーボン被覆率が高く、クロム酸
濃度が濃く、撹拌が激しく、しかも、電位走査速度が大
きく、温度が高くなる程、電流ピーク値は増大する。こ
のピーク電流は硫酸ソーダなどの添加により、通常のク
ロム酸イオンの拡散電流として観察することも出来る。The magnitude of the reduction peak current of chromic acid depends on the chromic acid concentration,
Since it varies depending on the stirring state of the solution, the potential scanning speed, the temperature, etc.,
It is necessary to perform measurement under these constant conditions in terms of reproducibility and accuracy. Generally, as the carbon coverage is high, the chromic acid concentration is high, the stirring is vigorous, the potential scanning speed is high, and the temperature is high, the current peak value increases. This peak current can also be observed as a normal chromate ion diffusion current by adding sodium sulfate or the like.
第7図に製造工程と組合せた本発明の実施例のフローシ
ィートを示す。図に示すように、管製造ライン11の途
中、例えば、脱脂洗浄部12または焼鈍装置(不活性ガ
ス製造装置を含む)部13より出た管の抜き取り14,
14′を行い、これを第1図に示したクロム酸溶液を納
めたセル15とポテンショメータ16の組合せ、及び表
面が清浄な材料を納めたセル(標準セル)17とポテン
ショメータ18の組合せによりそれぞれ還元電流を計測
し、ポテンショメータ16,18の出力の差、または比
を比較アンプ19によりとり、この値と潤滑油除去作
業、焼鈍作業工程により予め予測される因子、例えば、
洗浄油の汚れ、洗浄回数不足、温度……、不活性ガス製
造中の例えばメタン改質ではCH4 ++H2Oの(C/
H2O)比、触媒の老化、温度の不具合等の人工知能
(処理装置20,判断基準21)の出力22を製造ライ
ン11の脱脂洗浄部12および焼鈍装置部13に伝達
し、不合理を修正してゆく。尚、一度標準セル17の値
を人工知能側に記憶させれば、後は標準セル17とポテ
ンショメータ18は除去しても良い。FIG. 7 shows a flow chart of an embodiment of the present invention combined with a manufacturing process. As shown in the figure, in the middle of the pipe manufacturing line 11, for example, a pipe withdrawal 14 from a degreasing cleaning unit 12 or an annealing device (including an inert gas manufacturing device) unit 13,
14 'is carried out, and this is reduced by a combination of a cell 15 containing a chromic acid solution and a potentiometer 16 shown in FIG. 1 and a combination of a cell (standard cell) 17 containing a material with a clean surface and a potentiometer 18. The current is measured, and the difference or ratio between the outputs of the potentiometers 16 and 18 is taken by the comparison amplifier 19, and this value and a factor predicted in advance by the lubricating oil removal work and the annealing work process, for example,
Dirty wash oil, insufficient number of washes, the temperature ..., in for example methane reforming of inert gas produced CH 4 + + H 2 O in (C /
The output 22 of the artificial intelligence (processing device 20, judgment standard 21) such as H 2 O) ratio, catalyst aging, temperature defect, etc. is transmitted to the degreasing cleaning part 12 and the annealing device part 13 of the production line 11 to avoid irrationalities. I will fix it. Incidentally, once the value of the standard cell 17 is stored in the artificial intelligence side, the standard cell 17 and the potentiometer 18 may be removed thereafter.
また、本発明方法は測定対象としては、銅合金材のみに
限らず、鉄、銅、亜鉛、その他のクロム酸で不働態化す
る金属のカーボン汚染を検知する手段として有効であ
る。Further, the method of the present invention is not limited to the copper alloy material as a measurement target, but is effective as a means for detecting carbon contamination of iron, copper, zinc, and other metals that are passivated by chromic acid.
このように本発明は、金属材料素地を痛めず(腐蝕しな
い)しかも酸化作用があり、カーボン質表面では還元作
用の活発な溶液であるクロム酸溶液を基本とした電解液
中に被検査金属体を浸漬させ、その溶液中で金属を分極
させ、+0.6〜0V(銀/塩化銀電極基準)の電位域
に発生する還元電流の大きさを計測して、表面の清浄度
または汚染度を判定するようにしたものである。As described above, the present invention does not damage the metal material substrate (does not corrode), has an oxidizing action, and has a reducing action active on the carbonaceous surface. And then polarize the metal in the solution to measure the reduction current generated in the potential range of +0.6 to 0 V (based on silver / silver chloride electrode) to measure the cleanliness or contamination of the surface. The judgment is made.
カーボンは白金属類似の電気化学的挙動を示し、金属上
にこれが存在すると溶液中の酸化剤、例えば、海水中の
溶存酸素の還元反応の活性点として作用し、金属の溶解
即ち、腐蝕を異常に促進する。本発明は金属材製造工程
の監視や表面仕上げの程度の判定手段として従来ほとん
ど不可能であったものを、簡易にしかも単時間で判定す
ることが出来るようになり、金属材製造上、品質向上と
それによる製品プラントの腐蝕事故低減に大きく貢献す
ることが出来る。Carbon exhibits electrochemical behavior similar to white metal, and when it is present on a metal, it acts as an active point for the reduction reaction of an oxidant in a solution, for example, dissolved oxygen in seawater, and causes abnormal dissolution or corrosion of the metal. Promote to. INDUSTRIAL APPLICABILITY The present invention makes it possible to easily judge in a single time what has been almost impossible as a means for monitoring the metal material manufacturing process and judging the degree of surface finishing. And it can greatly contribute to the reduction of corrosion accidents in the product plant.
以上、詳述したように本発明によれば、簡単な方法によ
って鋭敏にその汚染度を判定することの出来る金属表面
の汚染度検出方法を提供することが出来る。As described above in detail, according to the present invention, it is possible to provide a method for detecting the degree of contamination of a metal surface, which can determine the degree of contamination sharply by a simple method.
第1図は本発明の一実施例を示すフローシィート、第2
図,〜第6図および第8図は各種材料の陰分極曲線を示
す図、第7図は本発明を適用した管製造工程の一例を示
すフローシィートである。 1……容器、2……クロム酸溶液、3……電磁撹拌機、
4……撹拌翼、5……供試材、6……対極、7……基準
電極、8a,〜8c……リード線、9……ポテンショス
タット。FIG. 1 is a flow chart showing an embodiment of the present invention.
FIGS. 6 to 8 show negative polarization curves of various materials, and FIG. 7 is a flow sheet showing an example of a tube manufacturing process to which the present invention is applied. 1 ... Container, 2 ... Chromic acid solution, 3 ... Magnetic stirrer,
4 ... Stirring blade, 5 ... Test material, 6 ... Counter electrode, 7 ... Reference electrode, 8a, 8c ... Lead wire, 9 ... Potentiostat.
Claims (1)
た、これらの間に配されて被検査金属との間に電位差を
与えるための基準電極を設けて被検査金属と基準電極と
の間に電位差を与えるとともに、これらをクロム酸溶液
に浸し、被検査金属と対極電極との間に流れる電流を計
測することにより、被検査金属についてクロム酸溶液を
ベースとした電解液中での電流を計測する計測工程と、 前記計測工程から得られた電流の状態から被検査金属の
清浄度または汚染度を判定する判定工程とを具備するこ
とを特徴とする金属表面の汚染度検出方法。1. A counter electrode and a reference electrode, which are arranged facing each other to the metal to be inspected, and which are provided between them to provide a potential difference with the metal to be inspected. And a potential difference between them, and soaking them in a chromic acid solution, and measuring the current flowing between the metal to be inspected and the counter electrode, the metal to be inspected in an electrolyte solution based on a chromic acid solution. And a determination step of determining the cleanliness or contamination degree of the metal to be inspected from the state of the current obtained from the measurement step. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61153550A JPH0612355B2 (en) | 1986-06-30 | 1986-06-30 | Metal surface contamination degree detection method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61153550A JPH0612355B2 (en) | 1986-06-30 | 1986-06-30 | Metal surface contamination degree detection method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS639858A JPS639858A (en) | 1988-01-16 |
| JPH0612355B2 true JPH0612355B2 (en) | 1994-02-16 |
Family
ID=15564958
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61153550A Expired - Lifetime JPH0612355B2 (en) | 1986-06-30 | 1986-06-30 | Metal surface contamination degree detection method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0612355B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN119438334B (en) * | 2024-09-27 | 2025-07-01 | 国网黑龙江省电力有限公司牡丹江水力发电总厂 | Concrete saturation sensor based on relative water contact area of fully polarized electrode and monitoring method |
-
1986
- 1986-06-30 JP JP61153550A patent/JPH0612355B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS639858A (en) | 1988-01-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Cruz et al. | AC impedance monitoring of pitting corrosion of stainless steel under a wet-dry cyclic condition in chloride-containing environment | |
| Mansfeld | The polarization resistance technique for measuring corrosion currents | |
| JP4141841B2 (en) | Sensor array and method for electrochemical corrosion monitoring | |
| US11892391B2 (en) | Field monitoring electrochemical method for anticorrosion performance of organic coatings in seawater environment | |
| Isaacs¹ et al. | Scanning reference electrode techniques in localized corrosion | |
| US7309414B2 (en) | Method for measuring localized corrosion rate with a multi-electrode array sensor | |
| WO1992016825A1 (en) | Method and apparatus for producing electrochemical impedance spectra | |
| Serebrennikova et al. | Visualization and characterization of electroactive defects in the native oxide film on aluminium | |
| Souto et al. | Uses of scanning electrochemical microscopy in corrosion research | |
| US5188715A (en) | Condensate corrosion sensor | |
| Bastos et al. | Localised measurements of pH and dissolved oxygen as complements to SVET in the investigation of corrosion at defects in coated aluminum alloy | |
| Wang et al. | The study of the varying characteristics of cathodic regions for defective coating in 3.5% sodium chloride solution by EIS and WBE | |
| JP2536364B2 (en) | Test piece | |
| JPH0612355B2 (en) | Metal surface contamination degree detection method | |
| CN110632134A (en) | A rapid detection method of chloride ion content on the surface of hot-rolled and pickled steel sheet | |
| He et al. | Real-time bulk acoustic wave studies of the inhibition behavior of mercaptobenzothiazole on copper | |
| JP2505460B2 (en) | Measuring device for surface cleanliness of metal pipes | |
| Court et al. | Electrochemical measurements of electroless nickel coatings on zincated aluminium substrates | |
| US5411648A (en) | Method and apparatus for on-line monitoring the quality of a purified metal sulphate solution | |
| JP3525230B2 (en) | Cooling water corrosion prevention measurement device | |
| JPS63259456A (en) | Corrosion rate measurement method | |
| JP3853250B2 (en) | Local corrosion sensor, local corrosion detection method and local corrosion detection apparatus using the local corrosion sensor | |
| Peter et al. | Electrochemical hydrogen permeation on steel sheets with in situ electrodeposition of a Pd layer at the exit side | |
| JP3777934B2 (en) | Method and apparatus for measuring corrosion in non-aqueous organic liquids | |
| Kuzmak et al. | A coulometric method for estimation of the anti-corrosion efficiency of polymer coatings |