JPH01254852A - Detection of corrosion - Google Patents
Detection of corrosionInfo
- Publication number
- JPH01254852A JPH01254852A JP8375588A JP8375588A JPH01254852A JP H01254852 A JPH01254852 A JP H01254852A JP 8375588 A JP8375588 A JP 8375588A JP 8375588 A JP8375588 A JP 8375588A JP H01254852 A JPH01254852 A JP H01254852A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- corrosion
- phase part
- conductivity
- vessel
- 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.)
- Pending
Links
- 238000005260 corrosion Methods 0.000 title claims abstract description 51
- 230000007797 corrosion Effects 0.000 title claims abstract description 51
- 238000001514 detection method Methods 0.000 title claims abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 229910052736 halogen Inorganic materials 0.000 claims abstract description 27
- 239000007791 liquid phase Substances 0.000 claims abstract description 23
- 150000002367 halogens Chemical class 0.000 claims abstract description 21
- 239000002184 metal Substances 0.000 claims abstract description 13
- 229910052751 metal Inorganic materials 0.000 claims abstract description 13
- -1 halogen ions Chemical class 0.000 claims abstract description 7
- 239000012071 phase Substances 0.000 claims description 16
- 239000007789 gas Substances 0.000 abstract description 42
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 abstract description 15
- 229910052740 iodine Inorganic materials 0.000 abstract description 15
- 239000011630 iodine Substances 0.000 abstract description 15
- 238000005259 measurement Methods 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 5
- 239000007792 gaseous phase Substances 0.000 abstract 6
- 150000002500 ions Chemical class 0.000 description 9
- 238000010586 diagram Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical compound II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 description 3
- 229910021645 metal ion Inorganic materials 0.000 description 3
- 238000012958 reprocessing Methods 0.000 description 3
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 2
- 229910052794 bromium Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 230000002285 radioactive effect Effects 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 239000002915 spent fuel radioactive waste Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000003758 nuclear fuel Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002123 temporal effect Effects 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Landscapes
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は金属材料の腐食検知方法に係り、特に原子力発
電プラントのハロゲン元素による腐食を判定するのに好
適な腐食検知方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for detecting corrosion of metal materials, and particularly to a method for detecting corrosion suitable for determining corrosion caused by halogen elements in nuclear power plants.
核燃料再処理工場は、使用済燃料を濃硝酸で溶解する溶
解工程において、NOxと共に使用済燃料中の放射性の
ヨウ素のIf (約10100ppや臭素Br、(約
10 p pm)の腐食性ガスが放出される。Nuclear fuel reprocessing plants release corrosive gases such as radioactive iodine If (approx. 10,100 ppm) and bromine Br (approx. 10 pp pm) in the spent fuel during the melting process in which spent fuel is dissolved with concentrated nitric acid. be done.
従来、このようなオフガスは第6図に示す処理装置によ
って処理される。第6図において、溶解槽21からのオ
フガスは、コンデンサ22に導入され、ここでオフガス
は90゛Cから40゛C程度まで冷却され、ガス中の大
部分の水分が凝縮し、除去される。Conventionally, such off-gas is processed by a processing device shown in FIG. In FIG. 6, the off-gas from the melting tank 21 is introduced into the condenser 22, where the off-gas is cooled from about 90°C to about 40°C, and most of the water in the gas is condensed and removed.
コンデンサ22からのオフガスは、NOx吸収塔24に
供給され、塔頂部から導入される吸収液(水)に吸収さ
れ、硝酸となって貯槽23に貯蔵される。The off-gas from the condenser 22 is supplied to the NOx absorption tower 24 , where it is absorbed by the absorption liquid (water) introduced from the top of the tower, becomes nitric acid, and is stored in the storage tank 23 .
貯槽23に貯溜された吸収酸中にはヨウ素Iz等が含ま
れており、これらのヨウ素等はヨウ素再追出塔25にて
ガス中に追い出される。ヨウ素再追出し塔25からのガ
ス中のヨウ素等は、ヨウ素除去塔26にて吸着・除去さ
れた後、NOxおよびヨウ素等が規定濃度以下となって
排気筒27より大気中に放出される。The absorbed acid stored in the storage tank 23 contains iodine Iz and the like, and these iodine and the like are expelled into the gas in the iodine re-expulsion tower 25. Iodine and the like in the gas from the iodine re-expulsion tower 25 is adsorbed and removed in the iodine removal tower 26, and then NOx, iodine, etc. are released into the atmosphere from the exhaust stack 27 with concentrations below a specified level.
この放射性のヨウ素I2や臭素Br、は他のハロゲン元
素の塩素CI!、tと同じように腐食性を有する元素で
あると同時に、その半減期が非常に長く、前記再処理オ
フガス系に長時間留まり、特に高湿度領域において腐食
による装置のリーク事故発生の要因となる。このため、
オフガス処理系においては運転期間中の機器の腐食の発
生・進展を検知する必要が生じるが、従来においては次
の検知方法等が用いられている。This radioactive iodine I2, bromine Br, and other halogen elements chlorine CI! It is a corrosive element like t, and at the same time has a very long half-life and remains in the reprocessing off-gas system for a long time, causing equipment leak accidents due to corrosion, especially in high humidity areas. . For this reason,
In off-gas treatment systems, it is necessary to detect the occurrence and progress of corrosion in equipment during operation, and conventionally the following detection methods have been used.
(])装置材料と同質の細線を装置内に挿入し、腐食に
よる断面減少によるオーム抵抗の増加により、腐食量を
検知する。(特開昭51−30783号公報)
(2)装置内の液を定期的に取り出し、その中の溶出し
た金属イオンの量を分析する。(特開昭60−4093
5号公報)
(3)試料金属の分極抵抗の変化を測定する。(特開昭
56−24551号公報)
〔発明が解決しようとする課題〕
従来の検知方法(1)〜(3)のうち、(1)の方法は
、腐食程度をリアルタイムに計測できる利点はあるが、
腐食形態として全面腐食しか検知できず、ハロゲンガス
に特徴的である孔食の発生・進展の予知には困難である
。(]) A thin wire of the same quality as the device material is inserted into the device, and the amount of corrosion is detected by the increase in ohmic resistance due to the reduction in cross section due to corrosion. (Japanese Unexamined Patent Publication No. 51-30783) (2) Periodically take out the liquid in the device and analyze the amount of metal ions eluted therein. (Unexamined Japanese Patent Publication No. 60-4093
(3) Measure the change in polarization resistance of the sample metal. (Japanese Unexamined Patent Publication No. 56-24551) [Problem to be solved by the invention] Among the conventional detection methods (1) to (3), method (1) has the advantage of being able to measure the degree of corrosion in real time. but,
Only general corrosion can be detected as a form of corrosion, and it is difficult to predict the occurrence and progress of pitting corrosion, which is characteristic of halogen gas.
(2)の方法は、液の定期的なサンプリングとその化学
分析より腐食の発生・進展の程度の予測ができるが、分
析に長い時間を要する。一方、(3)の方法は、取り扱
いが容易で連続的測定も可能であるが、適用環境が液中
のみであるため、ヨウ素ガスのようなハロゲン元素に対
しては、液中よりも腐食程度が厳しく、かつ液中では見
られない腐食生成物の付着を伴う気相環境での腐食の発
生・進展を検知することは困難である。Method (2) allows predicting the degree of corrosion occurrence and progress through periodic sampling of the liquid and chemical analysis thereof, but the analysis requires a long time. On the other hand, method (3) is easy to handle and allows for continuous measurement, but since the applicable environment is only in liquid, it is less corrosive than in liquid for halogen elements such as iodine gas. It is difficult to detect the occurrence and progress of corrosion in a gas phase environment where corrosion products are attached which are not seen in liquids.
本発明の目的は、上記した従来技術の課題を解決し、ハ
ロゲン元素を含む気液両環境でも連続計測が可能で腐食
の発生・進展を検知することができる腐食検知方法を提
供することにある。An object of the present invention is to solve the problems of the prior art described above, and to provide a corrosion detection method that can perform continuous measurement in both gas and liquid environments containing halogen elements and can detect the occurrence and progress of corrosion. .
本発明は、ヨウ素等ハロゲン元素を含む環境では、気相
中液滴および液相中の1.−イオン等が一定値に達した
時腐食が発生し、さらに腐食の進行と共に液中のI、−
イオンが自己増殖して行くことに着目した結果到達され
たもので、気相中液滴および液相中のI、−イオン濃度
の濃縮速度の経時的変化を液の伝導度測定から求め、腐
食環境下における金属の腐食の発生および進展を検知す
るようにしたものである。In an environment containing a halogen element such as iodine, the present invention can be applied to liquid droplets in the gas phase and 1. - Corrosion occurs when ions, etc. reach a certain value, and as the corrosion progresses, the I in the liquid, -
This was achieved by focusing on the self-propagation of ions, and the change over time in the concentration rate of I, - ions in droplets in the gas phase and in the liquid phase was determined by measuring the conductivity of the liquid. It is designed to detect the occurrence and progress of metal corrosion in the environment.
ヨウ素等ハロゲン元素を含む湿潤気相および液相での金
属の腐食減量は、第2図の60℃における材質5US3
04Lステンレス鋼の例かられかるように時間の経過に
より、加速的に増大を始める。The corrosion loss of metals in the wet gas phase and liquid phase containing halogen elements such as iodine is shown in Figure 2 for material 5US3 at 60°C.
As can be seen from the example of 04L stainless steel, it begins to increase rapidly over time.
一方、気相中液滴および液相中のI3−イオンの濃度も
第3図に示されるように腐食が開始されると、時間の経
過により加速的に濃縮し始める。On the other hand, as shown in FIG. 3, when corrosion starts, the concentration of I3- ions in the droplets in the gas phase and in the liquid phase begins to accelerate with the passage of time.
このI、−イオンの濃縮は次式により説明される。This concentration of I, - ions is explained by the following equation.
I ff ” +M (金属)→M !” +31−
・−・・−・(1)31− +31z−+ Is −
+21s−・・・・・・(2)(1)式は腐食の酸化・
還元反応であり、アノードではI、−イオンが金属Mを
酸化し、液相にM2゛イオンとして?8出させ、自らは
3モルのI−イオンに還元される。■−イオンには酸化
力がなく、それ以上金属を溶出できない。■、−イオン
はヨウ素12分子とI−イオンが結合した錯イオンであ
り、12部分が金属を腐食させる。I ff” +M (metal)→M!” +31-
・−・・−・(1) 31− +31z−+ Is −
+21s-...(2) Equation (1) is the oxidation of corrosion.
It is a reduction reaction, and I, - ions oxidize metal M at the anode, and M2' ions are formed in the liquid phase. 8, and itself is reduced to 3 moles of I- ion. -Ions have no oxidizing power and cannot elute metals any further. (2) - ions are complex ions in which 12 molecules of iodine and I- ions are combined, and the 12 parts corrode metals.
(2)式は3モルの■−イオンが常時補給されてくる1
2分子と結合し、3モルの13−イオンになる反応式で
あり、この平衡定数には約700と非常に大きく 、(
2)式の反応は瞬時に右方向に進行する。(2)式の右
辺の3モルの!、−イオンのうち、1モルの1.−イオ
ンは腐食が連続的に進行するために(1)式の反応に使
われるが、残りの2モルのI、″イオンが腐食サイクル
の進行と共に系に残留し、かつ腐食反応に関与すること
により、加速的な腐食減量およびI3−濃度の増大をも
たらすことになる。Equation (2) is 1 where 3 moles of ■-ions are constantly replenished.
This reaction formula combines two molecules to form 3 moles of 13-ion, and the equilibrium constant is very large at about 700.
2) The reaction in equation 2) instantly proceeds to the right. The 3 moles on the right side of equation (2)! , - ions, 1 mole of 1. -Ions are used in the reaction of equation (1) as corrosion progresses continuously, but the remaining 2 moles of I,'' ions remain in the system as the corrosion cycle progresses and participate in the corrosion reaction. This results in accelerated corrosion loss and increase in I3 concentration.
一方、液中で濃縮したI、−イオンの濃度は次式の伝導
度にの計測により、リアルタイムに検知される。On the other hand, the concentration of I, - ions concentrated in the liquid is detected in real time by measuring the conductivity according to the following equation.
ここで、kは伝導度(Ω/Cl11)、αは電離度、λ
、およびλ−は陽イオンおよび陰イオンの無限希釈度の
イオン伝導度(CT1/Ω・モル)、Cはイオン濃度(
モル/2)である。Here, k is conductivity (Ω/Cl11), α is ionization degree, λ
, and λ- are the ionic conductivities of cations and anions at infinite dilution (CT1/Ω·mol), and C is the ionic concentration (
mole/2).
α、λ。およびλ−はイオン種が定まれば、イオン濃度
Cの小さい範囲では一定となるので、伝導度にはI、−
イオン濃度に比例する。従って、伝導度にも時間の経過
と共に1.−濃度同様に加速的に増大することになる。α, λ. and λ- are constant in a small range of ion concentration C once the ion species is determined, so the conductivity includes I, -
Proportional to ion concentration. Therefore, with the passage of time, the conductivity also changes to 1. - The concentration will increase at an accelerated rate.
第4図にはその例を示す。An example is shown in FIG.
上記のように、経時的な腐食減量は、原理的には伝導度
の値の測定により検知可能であるが、実機内には初めか
ら別のイオン対が含まれていることがあり、そのため、
伝導度と時間の線図の形は変らないが絶対値レベルが上
昇する可能性がある。As mentioned above, corrosion loss over time can in principle be detected by measuring conductivity values, but other ion pairs may be included in the actual machine from the beginning, so
The shape of the conductivity vs. time diagram does not change, but the absolute value level may increase.
この問題は腐食量の検知に第5図に示されるような伝導
度の時間的勾配を用いることにより解決される。これは
、伝導度が腐食と共に、加速的に増大するため、その傾
きも一定値とならず、経時的に単純な増加カーブを示す
からである。This problem can be solved by using the temporal gradient of conductivity as shown in FIG. 5 to detect the amount of corrosion. This is because conductivity increases at an accelerating rate with corrosion, and its slope does not become a constant value, but instead shows a simple increasing curve over time.
また、計測した伝導度の値の中に腐食により溶出した金
属イオンの分も含まれているが、13−濃度と溶出金属
イオンの量の間には比例関係があるので、第4図は補正
を行うことにより、使用することができる。Also, the measured conductivity value includes metal ions eluted due to corrosion, but since there is a proportional relationship between the concentration and the amount of eluted metal ions, Figure 4 is corrected. It can be used by doing the following.
このように、各種構成機器の材質に対して、伝導度の経
時的測定を通して、金属の1.−等ノλロゲン元素を含
む液による腐食減量をリアルタイムに求め、腐食の発生
・進展を予知および警報することができる。In this way, through the measurement of conductivity over time for the materials of various component devices, the 1. - It is possible to determine the corrosion loss due to a liquid containing an iso-λ halogen element in real time, and to predict and warn the occurrence and progress of corrosion.
以下、本発明の実施例を図面に基づいて説明する。 Embodiments of the present invention will be described below based on the drawings.
第1図は本発明の腐食検知方法を実施するための装置の
系統図である。容器1の入口部より入ったヨウ素等ハロ
ゲンガスは液相部2を通過し、気相部3に出るが一部の
ガスは液相部2で吸収される。さらに気相部3に出たガ
スの1部は容器の内壁に付着した液滴に吸着されると同
時に、容器と同一材質で作られた計測用の気相部模擬液
相容器4内の約2cc以下の微量の液滴5にも吸収され
る。その他の大部分のハロゲンガスは容器出口部により
次の系に流出する。液相部2の液体および気相部3内の
気相部模擬液相容器4内の液滴5にはそれぞれ電極6が
設置され、液の伝導度は切り換えスイッチ7を通し、伝
導度計9で計測され、かつ記録計10で記録される。ま
た、伝導度測定回路は交番定電圧発生装置8により駆動
される。FIG. 1 is a system diagram of an apparatus for carrying out the corrosion detection method of the present invention. Halogen gas such as iodine that enters from the inlet of the container 1 passes through the liquid phase section 2 and exits into the gas phase section 3, but some of the gas is absorbed by the liquid phase section 2. Furthermore, part of the gas released into the gas phase part 3 is adsorbed by droplets attached to the inner wall of the container, and at the same time, about It is also absorbed by minute droplets 5 of 2 cc or less. Most of the other halogen gas flows out to the next system through the container outlet. Electrodes 6 are installed on each of the liquid in the liquid phase section 2 and the droplet 5 in the vapor phase simulated liquid phase container 4 in the gas phase section 3, and the conductivity of the liquid is measured through a changeover switch 7 and a conductivity meter 9. and recorded by the recorder 10. Further, the conductivity measurement circuit is driven by an alternating constant voltage generator 8.
さらに、伝導度計9にはバルブ切り損え用のリレー11
が接続され、このリレー11は伝導度計9の命令により
バルブ12およびバルブ13の開閉を行う。バルブ13
には1.ガス等のハロゲンガスバイパス配管14が接続
される。Furthermore, the conductivity meter 9 has a relay 11 for disconnecting the valve.
is connected, and this relay 11 opens and closes valves 12 and 13 according to commands from conductivity meter 9. Valve 13
There are 1. A halogen gas bypass pipe 14 such as gas is connected.
液相部2の液体内および気相部3内の気相模擬液相容器
4内の液滴内で?a1iIされたI、−等ハロゲンイオ
ンの濃度は切り換えスイッチ7により交互に伝導度計9
により計測され、記録計10で記録されると同時に、伝
導度の時間的勾配が予め設定された限界値を越えると伝
導度計9に接続された切り換え用リレー11が作動して
、バルブ12を閉に、またバルブ13を開にしてヨウ素
環/%ロゲンガスをハロゲンガスバイパス配管14を経
由して他の系に逃がし、容器へのハロゲンガスの流入を
断ち、容器の腐食の進行を防止する。In the liquid in the liquid phase part 2 and in the droplet in the gas phase simulated liquid phase container 4 in the gas phase part 3? The concentration of halogen ions such as I and -, which have been a1iI, is determined by the conductivity meter 9 alternately using the changeover switch 7.
When the time gradient of conductivity exceeds a preset limit value, the switching relay 11 connected to the conductivity meter 9 is activated to switch the valve 12 on. The valve 13 is closed and the valve 13 is opened to allow the iodine ring/% halogen gas to escape to other systems via the halogen gas bypass piping 14, thereby cutting off the flow of halogen gas into the container and preventing the progress of corrosion of the container.
上記のような検知方法では、腐食形態として孔食の発生
をも検知でき、かつ液の伝導度により腐食の発生および
進展を極めて簡便にかつ短時間に判定でき、しかも従来
困難であった気相環境下における腐食を検知することが
できる。With the above detection method, it is possible to detect the occurrence of pitting corrosion as a form of corrosion, and the occurrence and progress of corrosion can be determined extremely easily and in a short time based on the conductivity of the liquid. Corrosion in the environment can be detected.
なお、ヨウ素同様に第2図〜第5図に示す特性と類似の
特性を有する限り、他のノ\ロゲン元素を含むガスの気
相および液相下における金属の腐食の判定にも適用する
ことができることはいうまでもない。In addition, as with iodine, it can also be applied to the determination of corrosion of metals in the gas phase and liquid phase of gases containing other halogen elements, as long as they have properties similar to those shown in Figures 2 to 5. Needless to say, it can be done.
本発明によれば、ヨウ素等のノ\ロゲン元素を含む湿潤
気相および液相中での金属の腐食減量を腐食の進行と共
に増殖する液中■、″等のハロゲンイオンの濃度の増殖
速度の経時的変化を伝導度計測から求めることができる
ので、上記環境中での腐食の発生および進展状況を検知
することができる。According to the present invention, the corrosion loss of metal in a wet gas phase and liquid phase containing a halogen element such as iodine can be adjusted to increase the growth rate of the concentration of halogen ions in the liquid, such as Since changes over time can be determined from conductivity measurements, the occurrence and progress of corrosion in the above environment can be detected.
第1図は本発明の腐食検知方法を実施するための装置の
系統図、第2図は腐食減量と試験時間の関係を示す線図
、第3図はI、−イオン濃度と試験時間の関係を示す線
図、第4図は伝導度の腐食に伴う時間依存性を示す線図
、第5図は伝導度の時間変化率を示す線図、第6図は再
処理オフガス処理装置の系統図である。
2・・・・・・液相部、3・・・・・・気相部、4・・
・・・・気相部模擬液相容器、5・・・・・・液滴、6
・・・・・・電極、7・・・・・・切り換えスイッチ、
8・・・・・・交番定電圧発生装置、9・・・・・・伝
導度計、10・・・・・・記録計、14・・・・・・ハ
ロゲンガスバイパス管。
代理人 弁理士 西 元 勝 −
第4図 第5図
軽扇吟間t fhrl IX過吟聞t
fhr)第6図Fig. 1 is a system diagram of an apparatus for carrying out the corrosion detection method of the present invention, Fig. 2 is a diagram showing the relationship between corrosion weight loss and test time, and Fig. 3 is a diagram showing the relationship between I, -ion concentration and test time. Figure 4 is a diagram showing the time dependence of conductivity due to corrosion, Figure 5 is a diagram showing the rate of change of conductivity over time, and Figure 6 is a system diagram of the reprocessing off-gas treatment equipment. It is. 2...liquid phase part, 3...gas phase part, 4...
... Gas phase simulated liquid phase container, 5 ... Liquid droplet, 6
... Electrode, 7... Changeover switch,
8... Alternating constant voltage generator, 9... Conductivity meter, 10... Recorder, 14... Halogen gas bypass pipe. Agent Patent Attorney Masaru Nishimoto - Figure 4 Figure 5 Karougiginma t fhrl IX Karuginmon t
fhr) Figure 6
Claims (1)
食環境下において、腐食の発生・進展による気相中液滴
および液相中のハロゲンイオン濃度の経時的増殖に対し
、ハロゲンイオン濃度の増殖速度の経時的変化をハロゲ
ンイオンを含む液の伝導度を通して測定し、当該腐食環
境下における金属の腐食の発生および進展を検知するこ
とを特徴とする腐食検知方法。In a metal corrosive environment in a gas phase and liquid phase atmosphere containing halogen elements, the halogen ion concentration increases over time in droplets in the gas phase and in the liquid phase due to the occurrence and progress of corrosion. 1. A corrosion detection method characterized by measuring the change in velocity over time through the conductivity of a liquid containing halogen ions, and detecting the occurrence and progress of metal corrosion in the corrosive environment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8375588A JPH01254852A (en) | 1988-04-05 | 1988-04-05 | Detection of corrosion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8375588A JPH01254852A (en) | 1988-04-05 | 1988-04-05 | Detection of corrosion |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01254852A true JPH01254852A (en) | 1989-10-11 |
Family
ID=13811363
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8375588A Pending JPH01254852A (en) | 1988-04-05 | 1988-04-05 | Detection of corrosion |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01254852A (en) |
-
1988
- 1988-04-05 JP JP8375588A patent/JPH01254852A/en active Pending
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