JP2000258380A - Method and device for measuring erosion - Google Patents
Method and device for measuring erosionInfo
- Publication number
- JP2000258380A JP2000258380A JP11057941A JP5794199A JP2000258380A JP 2000258380 A JP2000258380 A JP 2000258380A JP 11057941 A JP11057941 A JP 11057941A JP 5794199 A JP5794199 A JP 5794199A JP 2000258380 A JP2000258380 A JP 2000258380A
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- JP
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- Prior art keywords
- erosion
- measuring
- electrochemical
- fluid
- noise
- 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.)
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- Testing Resistance To Weather, Investigating Materials By Mechanical Methods (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、エロージョンの測
定方法及びその測定装置に関する。詳しくは、エロージ
ョンによる酸化現象を電気化学的に捉え、その測定値に
基づきエロージョンによる減肉量を算出する方法及びそ
の測定装置に関する。本発明の方法により、石油化学プ
ラント等の機器及び配管装置類のエロージョンによる減
肉量を簡便に求めることができる。The present invention relates to a method and a device for measuring erosion. More specifically, the present invention relates to a method for electrochemically capturing an oxidation phenomenon due to erosion, and calculating a thinning amount due to erosion based on the measured value, and a measuring device therefor. According to the method of the present invention, it is possible to easily obtain the amount of thinning due to erosion of equipment such as a petrochemical plant and piping equipment.
【0002】[0002]
【従来の技術】石油化学プラント等の各種プラントは、
多くの機器及び配管装置類により構成されている。これ
らのプラントの健全性を保ち、且つ、安定した運転を行
うためには、これらの機器及び配管装置類の損害をなく
し、不具合を最小限に止めて、劣化管理及び診断を行な
い、保守管理をする必要がある。即ち、高い信頼性の下
で、長期的な安定した運転を維持していくためには、計
画的な予防保全が不可欠である。2. Description of the Related Art Various plants, such as petrochemical plants,
It is composed of many devices and piping devices. In order to maintain the soundness of these plants and to ensure stable operation, it is necessary to eliminate damage to these equipment and piping equipment, minimize problems, perform deterioration management and diagnosis, and perform maintenance management. There is a need to. That is, to maintain long-term stable operation under high reliability, planned preventive maintenance is indispensable.
【0003】機器及び配管装置類の主要な劣化要因の一
つとして、内部流体によって、管壁及び機器の内面等に
エロージョン・コロージョンによる薄肉化する減肉現
象、即ち、化学的作用による腐食(コロージョン)と機
械的作用による侵食(エロージョン)の相互作用により
生ずる減肉現象が発生する。一般に、これらの機器及び
配管装置類の減肉傾向の把握及び状況管理のため、石油
化学プラント等の実機プラントの機器及び配管装置類の
主な部位について、定期的に肉厚測定を超音波厚み計等
により実施している。[0003] One of the main deterioration factors of equipment and piping equipment is a thinning phenomenon in which the inner wall of the pipe wall and the inner surface of the equipment is thinned by erosion and corrosion due to internal fluid, that is, corrosion by chemical action (corrosion). ) And erosion due to mechanical action (erosion). Generally, in order to grasp the thinning tendency of these equipment and piping equipment, and to manage the situation, the thickness of the main parts of equipment and piping equipment of a real plant such as a petrochemical plant is regularly measured by ultrasonic thickness measurement. It is being implemented by the total.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上記の
方法では、相当長時間運転後、装置を停止した場合にし
か肉厚測定ができず、且つエロージョンのみによる減肉
量を測定することは困難である。本発明は、上記の実情
に鑑み、装置の内面の流体流れに伴うエロージョンによ
る減肉量を正確に測定する方法及びその測定装置を提供
することを目的とする。However, according to the above-mentioned method, it is impossible to measure the thickness only when the apparatus is stopped after the operation for a considerably long time, and it is difficult to measure the amount of thickness reduction by erosion alone. is there. The present invention has been made in view of the above circumstances, and has as its object to provide a method and an apparatus for accurately measuring the amount of wall thinning due to erosion accompanying a fluid flow on the inner surface of the apparatus.
【0005】[0005]
【課題を解決するための手段】本発明者は、機器及び配
管装置類の内部流体によるエロージョンによる減肉量の
測定法につき鋭意検討した結果、装置内の流体流れ中に
複数の装置材質と同じ材質の金属電極を浸漬し、該流体
の流速を変化させた場合に電気化学的電流ノイズ及び電
気化学的電位ノイズがそれぞれ変化し、その変化量より
エロージョンによる減肉量を測定できることを見出し、
本発明を完成するに至った。The inventor of the present invention has conducted intensive studies on a method of measuring the amount of wall thinning due to erosion caused by an internal fluid in equipment and piping equipment. When the metal electrode of the material is immersed, when the flow velocity of the fluid is changed, the electrochemical current noise and the electrochemical potential noise respectively change, and it is found that the thinning amount by erosion can be measured from the change amount.
The present invention has been completed.
【0006】即ち、本発明の要旨は、金属装置内を流れ
る流体中に金属装置と同じ材質を有する第1〜第3電極
を設け、流体の流速を変化させた場合の電気化学的電流
ノイズと電気化学的電位ノイズの変化をそれぞれ測定
し、演算処理によってエロージョンによる減肉量を算出
することを特徴とするエロージョンの測定方法、及び金
属装置と同じ材質を有する第1及び第2電極と、前記第
1〜第3電極を金属装置内を流れる流体中に取付ける取
付部材、前記第1電極と第2電極との間の電気化学的電
流ノイズを測定する電気化学的電流ノイズ測定手段、前
記第2電極と第3電極との間の電気化学的電位ノイズを
測定する電気化学的電位ノイズ測定手段、流体の流速を
変化させる手段、流速を変化させた場合の電気化学的電
流ノイズと電気化学的電位ノイズの変化をそれぞれ測定
し、演算処理によってエロージョンによる減肉量を算出
する手段とを備えることを特徴とするエロージョンの測
定装置、にある。That is, the gist of the present invention is to provide first to third electrodes having the same material as that of a metal device in a fluid flowing through the metal device, and to reduce electrochemical current noise when the flow velocity of the fluid is changed. The method of measuring erosion, characterized in that a change in electrochemical potential noise is measured, and the amount of wall thinning due to erosion is calculated by arithmetic processing, and the first and second electrodes having the same material as the metal device, and A mounting member for mounting the first to third electrodes in a fluid flowing through the metal device, an electrochemical current noise measuring means for measuring electrochemical current noise between the first electrode and the second electrode, Electrochemical potential noise measuring means for measuring electrochemical potential noise between the electrode and the third electrode, means for changing the flow rate of the fluid, electrochemical current noise and electrochemical when the flow rate is changed The change of the potential noise measured respectively, lying in the measuring device, erosion, characterized in comprising means for calculating the thickness reduction due to erosion by the processing.
【0007】[0007]
【発明の実施の形態】以下、本発明につき詳細に説明す
る。内部流体の装置内面のエロージョン・コロージョン
による減肉現象の発生のメカニズムを簡単に説明する。
エロージョン・コロージョンによる減肉現象は、先ず、
流体性状、温度等の化学的作用によりコロージョンが発
生し、これらは保護被覆の形成に関係する。また、流速
及び形状による機械的作用の機械的な力によりエロージ
ョンが発生し、これらの相互作用によりエロージョン・
コロージョンによる減肉現象が発生し、管壁及び機器の
内面等にエロージョン・コロージョンによる減肉現象が
発生する。このエロージョン・コロージョンによる減肉
現象及び作用について詳細に説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. The mechanism of the occurrence of the wall thinning phenomenon due to the erosion / corrosion of the inner surface of the internal fluid device will be briefly described.
The phenomenon of thinning due to erosion and corrosion is first
Corrosion occurs due to chemical actions such as fluid properties and temperature, which are related to the formation of a protective coating. In addition, erosion is generated by the mechanical force of the mechanical action due to flow velocity and shape, and erosion and
The wall thinning phenomenon due to the corrosion occurs, and the wall thinning phenomenon due to the erosion / corrosion occurs on the pipe wall and the inner surface of the device. The thinning phenomenon and action by the erosion and corrosion will be described in detail.
【0008】エロージョン・コロージョンによる減肉現
象は、化学的作用による腐食(コロージョン)と、機械
的作用による侵食(エロージョン)の相互作用により、
発生する減肉現象である。即ち、金属の減肉を考える場
合、周囲の流体条件(性状、温度等)及び流動条件(流
速、形状等)によりその機構が異なる。腐食環境下の金
属は腐食により、減肉していくが、流体の流速が小さい
等、機械的作用が小さい場合には単独腐食が起こり、機
械的作用がある程度以上大きくなると、腐食と共に侵食
の影響を受け、エロージョン・コロージョンによる減肉
現象が生じることになる。[0008] The thinning phenomenon due to erosion and corrosion is caused by the interaction between corrosion (corrosion) due to chemical action and erosion (erosion) due to mechanical action.
This is the phenomenon of wall thinning that occurs. That is, when considering metal thinning, the mechanism differs depending on the surrounding fluid conditions (properties, temperature, etc.) and flow conditions (flow speed, shape, etc.). Metals in a corrosive environment are reduced in thickness due to corrosion.However, if the mechanical action is small, such as a low flow velocity of the fluid, single corrosion occurs. As a result, a thinning phenomenon due to erosion and corrosion occurs.
【0009】本発明は金属装置の管壁や機器の内面を流
れる流体の流速を変化させた場合のエロージョン・コロ
ージョンによる減肉量の変化によりエロージョンによる
減肉量を測定することを特徴とするものである。即ち、
流体の流速が小さく、且つ機械的作用が小さい場合には
コロージョンによる単独腐食が起こり、一方、流体の流
速を大きくすると、エロージョンとコロージョンの両者
による減肉現象が生じる。この両者の差異を電気化学的
ノイズ法により測定し、エロージョンによる侵食に伴う
減肉量を測定するものである。The present invention is characterized in that the amount of wall thinning due to erosion is measured by the change in the amount of wall thinning due to erosion / corrosion when the flow velocity of the fluid flowing through the tube wall of the metal device or the inner surface of the equipment is changed. It is. That is,
When the flow velocity of the fluid is small and the mechanical action is small, the single corrosion due to the corrosion occurs. On the other hand, when the flow velocity of the fluid is increased, the thinning phenomenon occurs due to both the erosion and the corrosion. The difference between the two is measured by the electrochemical noise method, and the amount of thinning due to erosion is measured.
【0010】次に電気化学的ノイズ法による金属材料の
腐食測定法については、特開平9−297117号公報
に記載されている。図1において、被測定腐食性溶液中
に腐食測定対象となる金属表面の同一の材質の三個の測
定電極を浸漬する。第1の電極1と第2の電極2との間
に内部抵抗がほぼゼロの電流測定回路、いわゆる無抵抗
電流計4を接続させ、前記第2の電極2と第3の電極3
との間には、該電極側に影響を与えず信号電圧を測定し
得る電位計5が接続されている。Next, a method for measuring corrosion of a metal material by the electrochemical noise method is described in Japanese Patent Application Laid-Open No. 9-297117. In FIG. 1, three measurement electrodes of the same material on a metal surface to be measured for corrosion are immersed in a corrosive solution to be measured. A current measuring circuit having substantially zero internal resistance, that is, a so-called non-resistance ammeter 4 is connected between the first electrode 1 and the second electrode 2, and the second electrode 3 and the third electrode 3 are connected.
Between them, an electrometer 5 capable of measuring a signal voltage without affecting the electrode side is connected.
【0011】この状態では、電極1と電極2の間には、
それぞれ各電極表面の腐食の進行程度に応じたカップリ
ング電流が生じ、電流計4によってカップリング電流が
測定される。また、電極2と電極3の間の電位差は電位
計5によって測定される。図2は上記電流計4と電位計
5によって測定された電流、電位の変化を示したもので
ある。これらの測定結果より腐食率は下記式により算出
される。In this state, between the electrode 1 and the electrode 2,
A coupling current corresponding to the degree of progress of corrosion on each electrode surface is generated, and the coupling current is measured by the ammeter 4. The potential difference between the electrodes 2 and 3 is measured by the electrometer 5. FIG. 2 shows changes in current and potential measured by the ammeter 4 and the electrometer 5. From these measurement results, the corrosion rate is calculated by the following equation.
【0012】[0012]
【数1】 (Equation 1)
【0013】ここで、ΔEは電位の変化量 ΔIは電流の変化量 Rは腐食の電気化学的抵抗 をそれぞれ示すものである。Here, ΔE is the amount of change in potential, ΔI is the amount of change in current, and R is the electrochemical resistance of corrosion.
【0014】[0014]
【数2】腐食率=K×R[Equation 2] Corrosion rate = K × R
【0015】ここでKは金属材質と流体性状により決ま
る係数であり、金属試験片の腐食減量より逆算して求め
ることもできるし、また測定で求めることができる。本
発明においては、上記した腐食測定(電気化学的ノイズ
法)の原理を利用して図3に示すエロージョン測定装置
を用いて、図4に示す流体流れ中に取付けて流体の流速
を変化させた際の電気化学的電流ノイズと電気化学的電
位ノイズの変化を測定してエロージョンによる減肉量を
測定するものである。Here, K is a coefficient determined by the metal material and the fluid property, and can be obtained by calculating backward from the corrosion loss of the metal test piece or by measurement. In the present invention, the erosion measuring device shown in FIG. 3 was used in the fluid flow shown in FIG. 4 to change the flow velocity of the fluid using the erosion measuring device shown in FIG. 3 utilizing the principle of the above-described corrosion measurement (electrochemical noise method). The change in electrochemical current noise and electrochemical potential noise at that time is measured to measure the amount of thinning due to erosion.
【0016】図3において、1〜3は機器又は配管内面
と同じ材質の金属電極であり、それぞれの電極間は絶縁
物4′でシールされている。また電極2には流れる流体
の流速を変化させるために流体流れ方向に狭部を形成す
るオリフィス6が設けられており、該エロージョン測定
装置7はその両側に設けた取付部材(フランジ部材)8
によって配管又は装置に取付けられる。In FIG. 3, reference numerals 1 to 3 denote metal electrodes made of the same material as the inner surface of the equipment or the pipe, and the space between the electrodes is sealed with an insulator 4 '. The electrode 2 is provided with an orifice 6 which forms a narrow portion in the fluid flow direction in order to change the flow velocity of the flowing fluid, and the erosion measuring device 7 has mounting members (flange members) 8 provided on both sides thereof.
Attached to piping or equipment.
【0017】図4は、蒸気ドレンを排出するための配管
流れ中に上記エロージョン測定装置を取付け、バルブ9
の弁開度を調整して流体(蒸気)のオリフィス部6にお
ける流速を変化させた場合の電気化学的電流ノイズと電
気化学的電位ノイズを測定し、エロージョンによる減肉
量を算出する方法の概要を示すものであり、図5は、そ
の電気化学的電流ノイズと電気化学的電位ノイズの変化
を示したものである。これらのデータから下記式でエロ
ージョン減肉量を算出する。FIG. 4 shows a state in which the above-mentioned erosion measuring device is mounted in a pipe flow for discharging steam drain, and a valve 9 is provided.
Of the method of measuring the electrochemical current noise and the electrochemical potential noise when the flow rate of the fluid (steam) in the orifice section 6 is changed by adjusting the valve opening degree of the valve to calculate the amount of wall thinning due to erosion FIG. 5 shows changes in the electrochemical current noise and the electrochemical potential noise. From these data, the erosion thinning amount is calculated by the following equation.
【0018】[0018]
【数3】ER=EK*CR[Equation 3] ER = EK * CR
【0019】ここで、ERはオリフィスの減肉量により
算出されたエロージョン量 EKは測定結果により求めた係数 CRは腐食測定装置により算出された腐食量の合計Here, ER is the erosion amount calculated from the thickness of the orifice, EK is the coefficient obtained from the measurement result, and CR is the sum of the corrosion amounts calculated by the corrosion measuring device.
【0020】[0020]
【発明の効果】本発明によれば、装置内におけるエロー
ジョンによる酸化現象を電気化学的に捉え、これを測定
することにより、エロージョンによる減肉量を簡便に算
出することができる。According to the present invention, the oxidation phenomenon due to erosion in the apparatus is electrochemically detected and measured, whereby the thickness loss due to erosion can be easily calculated.
【図1】金属材料の腐食の電気化学的測定法の原理を示
す。FIG. 1 shows the principle of an electrochemical measurement method of corrosion of a metallic material.
【図2】電流及び電位の変化を示す図であるFIG. 2 is a diagram showing changes in current and potential.
【図3】本発明のエロージョン測定装置の断面図であ
る。FIG. 3 is a sectional view of the erosion measuring device of the present invention.
【図4】本発明のエロージョン測定方法の一例のフロー
図である。FIG. 4 is a flowchart of an example of the erosion measurement method of the present invention.
【図5】本発明のエロージョン測定方法における電流ノ
イズ及び電位ノイズの変化を示す図である。FIG. 5 is a diagram showing changes in current noise and potential noise in the erosion measurement method of the present invention.
1 電極 2 電極 3 電極 4 電流計 4′ 絶縁物 5 電位計 6 オリフィス 7 エロージョン測定装置 8 取付部材 9 バルブ Reference Signs List 1 electrode 2 electrode 3 electrode 4 ammeter 4 ′ insulator 5 electrometer 6 orifice 7 erosion measuring device 8 mounting member 9 valve
Claims (2)
同じ材質を有する第1〜第3電極を設け、流体の流速を
変化させた場合の電気化学的電流ノイズと電気化学的電
位ノイズの変化をそれぞれ測定し、演算処理によってエ
ロージョンによる減肉量を算出することを特徴とするエ
ロージョンの測定方法。1. A method according to claim 1, wherein the first to third electrodes having the same material as that of the metal device are provided in the fluid flowing through the metal device to reduce the electrochemical current noise and the electrochemical potential noise when the flow rate of the fluid is changed. A method for measuring erosion, characterized in that each change is measured and the amount of wall thinning due to erosion is calculated by arithmetic processing.
2電極と、前記第1〜第3電極を金属装置内を流れる流
体中に取付ける取付部材、前記第1電極と第2電極との
間の電気化学的電流ノイズを測定する電気化学的電流ノ
イズ測定手段、前記第2電極と第3電極との間の電気化
学的電位ノイズを測定する電気化学的電位ノイズ測定手
段、流体の流速を変化させる手段、流速を変化させた場
合の電気化学的電流ノイズと電気化学的電位ノイズの変
化をそれぞれ測定し、演算処理によってエロージョンに
よる減肉量を算出する手段とを備えることを特徴とする
エロージョンの測定装置。2. A first and a second electrode having the same material as a metal device, a mounting member for mounting the first to third electrodes in a fluid flowing through the metal device, and a mounting member for connecting the first and second electrodes. Electrochemical current noise measuring means for measuring electrochemical current noise between the electrodes; electrochemical potential noise measuring means for measuring electrochemical potential noise between the second electrode and the third electrode; Erosion characterized by comprising means for changing, and means for measuring changes in electrochemical current noise and electrochemical potential noise when the flow rate is changed, and calculating the erosion thinning amount by arithmetic processing. Measuring device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05794199A JP3760657B2 (en) | 1999-03-05 | 1999-03-05 | Erosion measuring method and measuring device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05794199A JP3760657B2 (en) | 1999-03-05 | 1999-03-05 | Erosion measuring method and measuring device |
Publications (2)
Publication Number | Publication Date |
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JP2000258380A true JP2000258380A (en) | 2000-09-22 |
JP3760657B2 JP3760657B2 (en) | 2006-03-29 |
Family
ID=13070072
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JP05794199A Expired - Fee Related JP3760657B2 (en) | 1999-03-05 | 1999-03-05 | Erosion measuring method and measuring device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001208713A (en) * | 2000-01-26 | 2001-08-03 | Mitsubishi Chemicals Corp | Method and apparatus for measuring corrosion in non- aqueous organic liquid |
JP2007017186A (en) * | 2005-07-05 | 2007-01-25 | Babcock Hitachi Kk | Calculation method of thinning rate of flow-accelerated corrosion, and diagnosis method of residual service life |
JP2018518685A (en) * | 2015-06-26 | 2018-07-12 | ローズマウント インコーポレイテッド | Corrosion rate measurement with multi-variable sensors |
-
1999
- 1999-03-05 JP JP05794199A patent/JP3760657B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001208713A (en) * | 2000-01-26 | 2001-08-03 | Mitsubishi Chemicals Corp | Method and apparatus for measuring corrosion in non- aqueous organic liquid |
JP2007017186A (en) * | 2005-07-05 | 2007-01-25 | Babcock Hitachi Kk | Calculation method of thinning rate of flow-accelerated corrosion, and diagnosis method of residual service life |
JP4630745B2 (en) * | 2005-07-05 | 2011-02-09 | バブコック日立株式会社 | Calculation method of flow accelerated corrosion thinning rate and remaining life diagnosis method |
JP2018518685A (en) * | 2015-06-26 | 2018-07-12 | ローズマウント インコーポレイテッド | Corrosion rate measurement with multi-variable sensors |
Also Published As
Publication number | Publication date |
---|---|
JP3760657B2 (en) | 2006-03-29 |
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