JPH07117355B2 - How to control dirt on copper alloy parts - Google Patents
How to control dirt on copper alloy partsInfo
- Publication number
- JPH07117355B2 JPH07117355B2 JP3063665A JP6366591A JPH07117355B2 JP H07117355 B2 JPH07117355 B2 JP H07117355B2 JP 3063665 A JP3063665 A JP 3063665A JP 6366591 A JP6366591 A JP 6366591A JP H07117355 B2 JPH07117355 B2 JP H07117355B2
- Authority
- JP
- Japan
- Prior art keywords
- potential
- copper alloy
- alloy member
- contamination
- iron film
- 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 - Fee Related
Links
- 229910000881 Cu alloy Inorganic materials 0.000 title claims description 49
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 220
- 229910052742 iron Inorganic materials 0.000 claims description 115
- 238000000034 method Methods 0.000 claims description 67
- 238000004140 cleaning Methods 0.000 claims description 41
- 238000011109 contamination Methods 0.000 claims description 39
- 239000000498 cooling water Substances 0.000 claims description 21
- 230000000694 effects Effects 0.000 claims description 8
- 238000005260 corrosion Methods 0.000 claims description 7
- 230000007797 corrosion Effects 0.000 claims description 7
- 238000000576 coating method Methods 0.000 claims description 6
- 230000009467 reduction Effects 0.000 claims description 6
- 230000005540 biological transmission Effects 0.000 claims description 5
- 239000011248 coating agent Substances 0.000 claims description 5
- 230000002238 attenuated effect Effects 0.000 claims description 4
- 238000005536 corrosion prevention Methods 0.000 claims description 3
- 230000002269 spontaneous effect Effects 0.000 description 16
- 238000010586 diagram Methods 0.000 description 11
- -1 iron ions Chemical class 0.000 description 10
- 238000005259 measurement Methods 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 238000007726 management method Methods 0.000 description 7
- 239000013535 sea water Substances 0.000 description 7
- 238000004210 cathodic protection Methods 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000003247 decreasing effect Effects 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- LFYJSSARVMHQJB-QIXNEVBVSA-N bakuchiol Chemical compound CC(C)=CCC[C@@](C)(C=C)\C=C\C1=CC=C(O)C=C1 LFYJSSARVMHQJB-QIXNEVBVSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 235000003891 ferrous sulphate Nutrition 0.000 description 2
- 239000011790 ferrous sulphate Substances 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 229910000936 Naval brass Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 229910001437 manganese ion Inorganic materials 0.000 description 1
- 230000028161 membrane depolarization Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
- Prevention Of Electric Corrosion (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は銅合金部材の汚れの管理
方法に関し、より詳しくは、海水等を冷却水として使用
する復水器、熱交換器等の設備における銅合金製の冷却
用管、管板等(以下、銅合金部材と称する)の表面に形
成するスライム等の汚れ具合を部分的にかつリアルタイ
ムに把握し、汚れを管理することができる方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling contamination of a copper alloy member, and more particularly to a copper alloy cooling pipe in equipment such as condensers and heat exchangers using seawater as cooling water. The present invention relates to a method capable of partially and in real time grasping the degree of dirt such as slime formed on the surface of a tube sheet or the like (hereinafter referred to as a copper alloy member) and managing the dirt.
【0002】[0002]
【従来の技術】海水を冷却水として使用する復水器、熱
交換器等の設備における銅合金部材の内面は、冷却水の
流れによってインレットアタックおよびデポジットアタ
ックといった腐食を生じやすい。そこでこのような腐食
の抑制手段として、外部電源方式等による電気防食法
と、冷却水中に鉄イオンを供給して銅合金部材の表面に
鉄皮膜を形成させる方法との併用が近年広く実施されて
いる。2. Description of the Related Art The inner surface of a copper alloy member in facilities such as condensers and heat exchangers that use seawater as cooling water is apt to be corroded by inlet water flow and deposit attack due to the flow of cooling water. Therefore, as a means for suppressing such corrosion, a combination of a cathodic protection method such as an external power supply method and a method of supplying iron ions into cooling water to form an iron film on the surface of a copper alloy member has been widely used in recent years. There is.
【0003】しかし、係る設備にあっては、冷却水とし
て海水等を使用するので、冷却水中の微生物(通常、プ
ランクトン)や海底面から浮遊するマンガンイオン等が
銅合金部材の内面に付着し(一般に総称としてスライム
と呼ばれる)、鉄皮膜の防食効果の低下や設備の熱貫流
効率の低下を招く等の問題が生じる。However, in such equipment, since seawater or the like is used as cooling water, microorganisms (usually plankton) in the cooling water and manganese ions floating from the sea bottom adhere to the inner surface of the copper alloy member ( (Generally referred to as slime), there is a problem such as a decrease in the anticorrosion effect of the iron film and a decrease in the heat transmission efficiency of the equipment.
【0004】そこでこのようなスライム等による部材の
汚れを軟質ボール洗浄、硬質ボール洗浄、ジェット洗
浄、ブラシ洗浄等の洗浄方法によって適宜除去する必要
がある。しかしブラシ洗浄またはジェット洗浄を行なう
には設備を長期(数日)に亘って休止する必要があり、
また軟質ボール洗浄および硬質ボール洗浄は運転中でも
可能であるが洗浄評価については設備を一時休止する必
要がある。さらに上記汚れの発生状況は水温、季節等の
様々な要因の影響を受けやすく、規則性がない。Therefore, it is necessary to appropriately remove stains on the member due to such slime by a cleaning method such as soft ball cleaning, hard ball cleaning, jet cleaning and brush cleaning. However, in order to perform brush cleaning or jet cleaning, it is necessary to stop the equipment for a long time (several days),
Also, soft ball cleaning and hard ball cleaning can be performed during operation, but it is necessary to suspend the equipment for cleaning evaluation. Furthermore, the above-mentioned stain generation condition is susceptible to various factors such as water temperature and season, and is not regular.
【0005】そのため、洗浄に要する設備の休止期間を
できるだけ少なくし、係る銅合金部材の汚れを効果的に
洗浄すべく、汚れの状態を適格にかつ設備を休止せずに
把握しておく必要がある。Therefore, in order to minimize the downtime of the equipment required for cleaning and to effectively clean the dirt of the copper alloy member concerned, it is necessary to grasp the condition of dirt properly and without stopping the equipment. is there.
【0006】ところが、汚れの状態を目視により把握す
るには設備を休止せねばならず、定量的な判断もできな
い。また、係る付着物を採集して分析し、その結果を得
るには相当の日時と手間がかかり、しかも採集の際に設
備を休止しなければならないので、付着物量から汚れの
状態を直接把握することも困難である。However, in order to visually grasp the state of dirt, the equipment must be stopped, and a quantitative judgment cannot be made. In addition, it takes a considerable amount of time and effort to collect and analyze the deposits and obtain the results, and since the equipment must be stopped during the collection, the state of dirt can be directly grasped from the amount of deposits. Is also difficult.
【0007】このような汚れの把握方法として真空度偏
差値を利用する方法が従来から一般的に使用されてい
る。係る方法は、銅合金部材に汚れが付着すると熱貫流
効率の低下を生じ、発電プラント等の設備の蒸気側の真
空度に影響することを利用して、真空度偏差値から汚れ
の状態を把握する方法であり、真空度偏差値が汚れの程
度と密接な関係があることは経験的に見出されている。
係る真空度偏差値は(実測真空度)−(予想真空度)の
値であり、予想真空度は設備の容量、ポンプ数、冷却水
温等に基づいて設備ごとに演算で求める値である。As a method of grasping such dirt, a method of utilizing a vacuum deviation value has been generally used conventionally. This method uses the fact that if the copper alloy member is contaminated with dirt, it causes a reduction in heat transmission efficiency and affects the degree of vacuum on the steam side of equipment such as a power plant. It has been empirically found that the vacuum degree deviation value is closely related to the degree of contamination.
The vacuum degree deviation value is a value of (measured vacuum degree)-(estimated vacuum degree), and the expected vacuum degree is a value calculated by each facility based on the capacity of the facility, the number of pumps, cooling water temperature, and the like.
【0008】ところで、復水器、熱交換器等の設備は通
常複数の熱交換ユニット(コンデンサー;各ユニットは
一般に複数の冷却用管と2つの水室を具備する)を具備
しており、ユニット毎に汚れの状態は異なることが分か
っている。しかしながら、上記真空度偏差値を利用する
方法の場合、上記設備の蒸気側は通常設備全体で一つと
なっていることから、設備全体で平均的にしか汚れの状
態を把握することができない。そのため従来は、設備の
一部ユニットに汚れが集中した場合には検知し辛く、本
来なら一ユニットのみを早期に軟質ボール洗浄等すれば
足りる場合であっても、結果的に全ユニットをブラシ洗
浄せざるを得なくなることがあった。By the way, facilities such as a condenser and a heat exchanger are usually provided with a plurality of heat exchange units (condenser; each unit is generally provided with a plurality of cooling pipes and two water chambers). It is known that the state of dirt is different for each. However, in the case of using the above-mentioned vacuum degree deviation value, since the steam side of the equipment is usually one in the whole equipment, the state of contamination can be grasped only on average in the whole equipment. Therefore, conventionally, it is difficult to detect when dirt is concentrated on a part of the equipment, and even if it is sufficient to wash only one unit with a soft ball early, as a result, all units are brush-washed as a result. There were times when I was forced to do so.
【0009】[0009]
【発明が解決しようとする課題】本発明は上記従来技術
の問題に鑑みて成されたものであり、海水等を冷却水と
して使用する復水器、熱交換器等の設備における銅合金
部材の表面に形成するスライム等の汚れ具合を該設備の
ユニット毎にかつリアルタイムに把握し、その汚れを管
理することによって、該設備を効率的に適正稼働状態に
維持することが可能な方法を提供することを目的とする
ものである。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art, and relates to a copper alloy member in equipment such as condensers and heat exchangers that use seawater or the like as cooling water. Provided is a method capable of efficiently maintaining the equipment in an appropriate operating state by grasping the degree of dirt such as slime formed on the surface for each unit of the equipment in real time and managing the dirt. That is the purpose.
【0010】[0010]
【課題を解決するための手段および作用】本発明者らは
上記課題を解決すべく鋭意研究した結果、銅合金部材の
自然電位が該銅合金部材の汚れの程度と非常に密接な関
係があることを見出し、本発明に到達した。Means and Actions for Solving the Problems As a result of intensive studies conducted by the present inventors to solve the above problems, the spontaneous potential of the copper alloy member has a very close relationship with the degree of contamination of the copper alloy member. The inventors have found that and reached the present invention.
【0011】すなわち、本発明の銅合金部材の汚れの管
理方法は、冷却水を必要とする設備に使用される銅合金
部材を電気防食法と該部材の表面に鉄皮膜を形成させる
ことによる防食法とを併用して防食する際における該銅
合金部材の汚れの管理において、該冷却水中に設けた電
極から該冷却水を通じて該銅合金部材に通電する電流回
路と、該銅合金部材の電位を測定する電位測定回路とを
有する通電装置を用いて、該通電を一時的に遮断した後
に陰極(銅合金部材)電位が減衰して安定するところの
自然電位を求める工程と、該自然電位を予め定められた
基準値と比較する工程と、該自然電位が該基準値より貴
になると該銅合金部材の汚れを洗浄する工程とからなる
ことを特徴とする方法である。That is, the method for controlling the contamination of a copper alloy member of the present invention is a method for preventing corrosion of a copper alloy member used for equipment that requires cooling water by performing an anticorrosion method and forming an iron film on the surface of the member. In controlling the contamination of the copper alloy member during corrosion prevention in combination with the method, a current circuit for energizing the copper alloy member from the electrode provided in the cooling water through the cooling water and the potential of the copper alloy member Using a current-carrying device having a potential measuring circuit for measuring, a step of obtaining a natural potential at which the potential of the cathode (copper alloy member) is attenuated and stabilized after the current is temporarily cut off, and the natural potential is previously set. The method is characterized by comprising a step of comparing with a predetermined reference value and a step of cleaning dirt of the copper alloy member when the natural potential becomes nobler than the reference value.
【0012】本発明の対象となる銅合金部材は、表面が
海水、淡水等の冷却水と接しており、電気防食法と鉄皮
膜による防食法とを併用して防食されているものであ
る。上記の電気防食法および鉄皮膜による防食法はいず
れも特に制限されない。例えば、鉄皮膜による防食法と
しては硫酸第1鉄溶液の導入あるいは鉄電極を用いた鉄
電解法等によって鉄皮膜形成用の鉄イオンを供給する方
法がある。The copper alloy member which is the object of the present invention has its surface in contact with cooling water such as seawater or fresh water, and is protected from corrosion by using both the anticorrosion method and the corrosion prevention method using an iron coating. The above-mentioned cathodic protection method and anticorrosion method using an iron film are not particularly limited. For example, as an anticorrosion method using an iron film, there is a method of supplying iron ions for forming an iron film by introducing a ferrous sulfate solution or an iron electrolysis method using an iron electrode.
【0013】本発明において汚れの程度の指標として求
める自然電位は、通電していない時の銅合金部材(陰
極)の電位(復極安定電位)であり、すなわち通電を遮
断した後に減衰して安定したところの陰極電位である。
通常、陰極電位が真の自然電位になるには通電遮断後約
5分間を要する。In the present invention, the natural potential obtained as an index of the degree of contamination is the potential of the copper alloy member (cathode) when not energized (depolarization stable potential), that is, it is attenuated and stabilized after the energization is cut off. It is the cathode potential of the place where it did.
Usually, it takes about 5 minutes after the power supply is cut off for the cathode potential to reach the true natural potential.
【0014】本発明にあっては上記自然電位を実際に測
定してもよいが、電気防食の効果および測定作業上の観
点から、通電遮断時間をできるだけ短縮して自然電位を
得ることが好ましく、下記式(1) En=E60+(E60−E50) (1) [式(1)中、Enは自然電位、E50は通電を遮断し
てから50秒後の陰極電位、E60は通電を遮断してか
ら60秒後の陰極電位をそれぞれ示す]に基づいて求め
ることが最も好ましい。下記式(1)に基づいて求めた
自然電位は実測した値と略一致するので、この方法によ
って約1分で自然電位を求めることが可能である。In the present invention, the above-mentioned spontaneous potential may be actually measured, but from the viewpoint of the effect of anticorrosion and measurement work, it is preferable to shorten the energization interruption time as much as possible to obtain the spontaneous potential. The following formula (1) En = E 60 + (E 60 −E 50 ) (1) [In the formula (1), En is a natural potential, E 50 is a cathode potential after 50 seconds from interruption of energization, E 60 Is the cathode potential 60 seconds after the power supply is cut off.] Is most preferable. Since the natural potential calculated based on the following equation (1) substantially matches the actually measured value, it is possible to calculate the natural potential in about 1 minute by this method.
【0015】また、本発明において用いる通電装置は、
冷却水中に設けた電極から冷却水を通じて銅合金部材に
通電する電流回路と、銅合金部材の電位を測定する電位
測定回路とを有するものであればよく、外部電源方式に
よる電気防食装置を兼ねたものであると装置が煩雑とな
らないので好ましい。また、かかる通電装置を電気防食
装置と別に設けてもよい。なお、対象とする設備が複数
のユニットからなるものである場合は、上記通電装置を
ユニット毎に設けて各ユニットにおける自然電位を求め
ることが好ましい。The energizing device used in the present invention is
As long as it has a current circuit for energizing the copper alloy member from the electrode provided in the cooling water through the cooling water and a potential measuring circuit for measuring the potential of the copper alloy member, it can also serve as a cathodic protection device by an external power supply method. It is preferable to use one because the apparatus does not become complicated. Further, such an energization device may be provided separately from the cathodic protection device. When the target equipment is composed of a plurality of units, it is preferable that the energizing device is provided for each unit to obtain the natural potential of each unit.
【0016】本発明にあっては、上記自然電位を予め定
められた基準値と比較し、自然電位が基準値より貴の場
合は銅合金部材の汚れを洗浄する。上記基準値は操業条
件や環境条件等によって変化するので一律に定めること
は困難であり、設備毎あるいはそのユニット毎に設定す
る必要がある。上記基準値の設定にあたっては、前記鉄
皮膜の防食効果の低下および/または前記設備の熱貫流
効率の低下が許容範囲を超えないように経験的に定める
ことが好ましい。具体的には例えば、銅合金部材への付
着物量を一定期間測定してそのデータから設定しても良
く、また上記従来の真空度偏差値を参考にして設定して
もよい。そして、設備をより厳しく管理する場合は基準
値をより卑の値に設定するようにすればよい。また、上
記基準値を自然電位のバラツキ等を見越してある程度の
幅をもって設定し、その範囲に入ったら洗浄の準備を
し、その範囲より貴となったら直ちに洗浄するようにし
てもよい。In the present invention, the natural potential is compared with a predetermined reference value, and when the natural potential is nobler than the reference value, the copper alloy member is cleaned. Since the above-mentioned reference value changes depending on operating conditions, environmental conditions, etc., it is difficult to set it uniformly, and it is necessary to set it for each equipment or each unit. In setting the above-mentioned reference value, it is preferable to empirically determine such that the reduction of the anticorrosion effect of the iron coating and / or the reduction of the heat transmission efficiency of the equipment does not exceed the allowable range. Specifically, for example, the amount of deposits on the copper alloy member may be measured for a certain period of time and set from the data, or may be set with reference to the conventional vacuum degree deviation value. When the equipment is to be managed more strictly, the reference value may be set to a more base value. Further, the above reference value may be set with a certain width in consideration of variations in the natural potential, and cleaning may be performed when the value falls within the range, and cleaning may be performed immediately when the value becomes higher than the range.
【0017】また、前記の汚れを洗浄する方法は特に制
限されず、汚れの程度等に応じて選択されるが、設備の
休止期間が短くてすむ(数時間)ことから軟質ボール洗
浄または硬質ボール洗浄が好ましく、良好な鉄皮膜を除
去する危険性が少ない軟質ボール洗浄が最も好ましい。The method for cleaning the dirt is not particularly limited and may be selected according to the degree of dirt, etc., but the equipment can be used for a short period of time (several hours), so soft ball cleaning or hard ball cleaning is possible. Washing is preferred, and soft ball washing is most preferred, with less risk of removing good iron coatings.
【0018】以上説明した本発明の銅合金部材の汚れの
管理方法は、それだけでも充分に汚れの管理が可能であ
るが、もちろんより慎重を期すために従来の真空度偏差
値を利用する方法等と併せて行なってもよい。Although the above-described method for controlling the contamination of the copper alloy member of the present invention can sufficiently control the contamination, of course, in order to be more careful, the conventional method of utilizing the deviation value of the degree of vacuum is used. You may perform it together with.
【0019】また、本発明の銅合金部材の汚れの管理方
法を、本出願人らによる鉄皮膜抵抗の計測方法(特開昭
59−147247号公報)と併せて用いるとなお好ま
しい。この鉄皮膜抵抗の計測方法は、銅合金部材表面に
形成される鉄皮膜の抵抗値測定に際し、重畳されて計測
される鉄皮膜抵抗値(Rf)、分極抵抗値(Rd)および測
定上のIR降下分を含んだ第3成分抵抗値(Rx)から鉄
皮膜抵抗値(Rf)のみを分離して計測することを可能と
し、係る鉄皮膜抵抗値(Rf)に基づいて鉄皮膜の状態を
把握できるようにする方法である。Further, it is more preferable to use the method for controlling the contamination of the copper alloy member of the present invention together with the method for measuring the resistance of the iron film by the present applicants (Japanese Patent Application Laid-Open No. 59-147247). This method for measuring the resistance of the iron film is such that, when measuring the resistance value of the iron film formed on the surface of the copper alloy member, the iron film resistance value (Rf), the polarization resistance value (Rd), and the measured IR are superimposed and measured. It is possible to separate and measure only the iron film resistance value (Rf) from the third component resistance value (Rx) including the drop, and grasp the state of the iron film based on the iron film resistance value (Rf). It's a way to be able to.
【0020】すなわち、上記鉄皮膜抵抗の計測方法は、
冷却水を必要とする設備に使用される銅合金部材を電気
防食法と該部材の表面に鉄皮膜を形成させることによる
防食法とを併用して防食する際における該防食用鉄皮膜
の管理において、電流測定回路と電位測定回路とを有す
る通電装置を用いて、通電時の陰極電位と通電電流値I
とを測定する工程と、通電を一時的に遮断し、減衰して
いく陰極電位を、該陰極電位が安定するところの自然電
位になるまで若しくは該自然電位の予測が可能になるま
で測定する工程と、該通電遮断後の陰極電位と該自然電
位との差である電位変化値Vを通電を遮断してからの時
間ごとに求める工程と、該電位変化値の対数logVの
時間に対する減衰曲線(イ)を得る工程と、該減衰曲線
(イ)が指数的な減少傾向から直線的な減少傾向に移行
した後の、該対数logVの時間に対する回帰直線
(ロ)を求める工程と、該減衰曲線(イ)と該回帰直線
(ロ)との差である鉄皮膜抵抗成分電位Vf を通電を遮
断してからの時間ごとに求める工程と、該鉄皮膜抵抗成
分電位Vf の対数logVfの時間に対する回帰直線
(ハ)を求める工程と、該回帰直線(ハ)から通電を遮
断した瞬間の鉄皮膜抵抗成分電位Vf(t=0)を求める工程
と、得られた鉄皮膜抵抗成分電位Vf (t=0) および通電
電流値Iを用いて下記式 Rf ={Vf(t=0)/I}×{S/K} [式中、Rf は鉄皮膜抵抗値、Sは通電対象面積、Kは
通電電流配分比率をそれぞれ示す]から鉄皮膜抵抗値R
f を求める工程とからなることを特徴とする方法であ
る。そして、上記鉄皮膜抵抗値Rf は鉄皮膜の状態と密
接な関係があることを利用して鉄皮膜抵抗値Rf から鉄
皮膜の状態を把握し、通電電流量の調節等によって鉄皮
膜の管理を可能とする方法である。That is, the method for measuring the iron film resistance is as follows.
In the control of the anticorrosion iron film when the anticorrosion method is used in combination with the anticorrosion method and the anticorrosion method by forming the iron film on the surface of the copper alloy member used for equipment requiring cooling water Using an energizing device having a current measuring circuit and a potential measuring circuit, the cathode potential and energizing current value I during energization
And a step of measuring the cathodic potential, which is temporarily cut off and attenuated, until the cathodic potential reaches a natural potential at which the cathodic potential is stable or until the natural potential can be predicted. And a step of obtaining a potential change value V, which is a difference between the cathode potential after the power supply is cut off and the natural potential, at each time after the power supply is cut off, and an attenuation curve with respect to a time of logarithm logV of the potential change value ( A), a step of obtaining a regression line (b) with respect to time of the logarithm logV after the attenuation curve (a) has changed from an exponential decreasing tendency to a linear decreasing tendency, and the attenuation curve The step of obtaining the iron film resistance component potential Vf, which is the difference between (a) and the regression line (b), at each time after the current is cut off, and the regression with respect to the time of the logarithm logVf of the iron film resistance component potential Vf. A step of obtaining a straight line (C), Using the process of obtaining the iron film resistance component potential Vf (t = 0) at the moment when the energization is cut off from the return line (C) and the obtained iron film resistance component potential Vf (t = 0) and the energization current value I From the following formula Rf = {Vf (t = 0) / I} × {S / K} [in the formula, Rf is the resistance value of the iron film, S is the area to be energized, and K is the distribution ratio of the energized current] Resistance value R
and a step of obtaining f. The iron film resistance value Rf is closely related to the iron film state, so the iron film resistance value Rf is used to grasp the state of the iron film, and the iron film can be controlled by adjusting the amount of energizing current. This is a possible method.
【0021】なお、上記鉄皮膜抵抗の計測方法にあって
はその過程で自然電位を求めているが、その自然電位が
汚れの程度と密接な関係があることは全く見出されてお
らず、単に鉄皮膜抵抗値Rf を求めるために必要な値で
あった。In the above method of measuring the resistance of the iron film, the spontaneous potential is obtained in the process, but it has not been found that the spontaneous potential is closely related to the degree of contamination. It was a value merely required for obtaining the iron film resistance value Rf.
【0022】このような鉄皮膜抵抗の計測方法と本発明
の銅合金部材の汚れの管理方法とを併せて行なうことに
よって、自然電位から汚れの管理が、さらに鉄皮膜抵抗
値Rf から鉄皮膜の状態の把握が同一の装置でしかも同
時に可能となり、設備をより効率的に適正稼働状態に維
持することが可能となる。By performing such a method for measuring the resistance of the iron film and the method for controlling the contamination of the copper alloy member of the present invention, the contamination can be controlled from the natural potential, and the resistance of the iron coating can be determined from the resistance Rf of the iron coating. The state can be grasped by the same device and at the same time, and the equipment can be more efficiently maintained in the proper operating state.
【0023】以下、本発明の銅合金部材の汚れの管理方
法と上記鉄皮膜抵抗の計測方法とを併せて行なう場合を
例にとって図面を参照してより詳細に説明する。Hereinafter, the case where the method for controlling the contamination of the copper alloy member of the present invention and the method for measuring the iron film resistance are performed together will be described in more detail with reference to the drawings.
【0024】図1は電気防食法として外部電源方式によ
る防食法を実施する復水器において本発明の管理方法を
実施するための通電装置の一例を示すブロック図であ
る。FIG. 1 is a block diagram showing an example of an energizing device for carrying out the control method of the present invention in a condenser for carrying out an anticorrosion method by an external power supply method as an anticorrosion method.
【0025】図1において、水室5内には通電用の電極
1、並びに管板面2および冷却管3(銅合金部材)の電
位を検出するための亜鉛基準電極4が設置されている。
そして、直流電源装置6は電流測定回路(同図中のA)
および電位測定回路(同図中のE)を有するものであ
り、基準電極4によって照合させた適正電位を維持する
ように通電電流の調整を行なうようになっている。ま
た、図1中の7は後述する計測装置である。さらに、図
示はしないが、上記復水器には鉄電解装置、硫酸第一鉄
の導入装置、あるいは鉄電極を設ける等して鉄イオンを
冷却水中に供給するようになっている。In FIG. 1, an electrode 1 for energization and a zinc reference electrode 4 for detecting the potentials of the tube plate surface 2 and the cooling pipe 3 (copper alloy member) are installed in a water chamber 5.
The DC power supply 6 is a current measuring circuit (A in the figure).
And a potential measuring circuit (E in the figure), and the energizing current is adjusted so as to maintain the proper potential checked by the reference electrode 4. Further, 7 in FIG. 1 is a measuring device described later. Further, although not shown, an iron electrolysis device, a ferrous sulfate introduction device, or an iron electrode is provided in the condenser to supply iron ions into the cooling water.
【0026】本発明の銅合金部材の汚れの管理方法を実
施するにあたっては、通電を一時的に遮断した後に上記
電位測定回路によって上記自然電位が測定される。ま
た、自然電位を上記式(1)に基づいて求める場合は、
通電を遮断してから50秒後と60秒後の陰極電位を上
記電位測定回路によって測定し、それらのデータから計
測装置7によって自然電位が求められる。そして計測装
置7によって上記自然電位を予め定められた基準値と比
較し、自然電位が基準値より貴になった場合に銅合金部
材の汚れを洗浄する手段(図示せず)を作動させる。洗
浄手段を作動させる手段は特に制限されず、係る場合に
信号を発するようにしておき、手動的に洗浄手段を作動
させても、あるいは自動的に作動させてもよい。In carrying out the method for controlling contamination of a copper alloy member according to the present invention, the spontaneous potential is measured by the potential measuring circuit after the current is temporarily cut off. When the natural potential is calculated based on the above equation (1),
The cathode potential 50 seconds and 60 seconds after the power supply is cut off is measured by the potential measuring circuit, and the natural potential is obtained by the measuring device 7 from the data. Then, the measuring device 7 compares the natural potential with a predetermined reference value, and when the natural potential becomes nobler than the reference value, a means (not shown) for cleaning the contamination of the copper alloy member is activated. The means for activating the cleaning means is not particularly limited, and a signal may be generated in such a case, and the cleaning means may be manually activated or automatically activated.
【0027】また、上記鉄皮膜抵抗の計測方法を併せて
行なう場合は、上記電流測定回路および電位測定回路に
よって通電時の陰極電位、通電電流値Iおよび通電遮断
後の陰極電位を測定し、それらのデータから計測装置7
によって鉄皮膜抵抗値Rf が求められる。When the above-mentioned iron film resistance measuring method is also performed, the current measuring circuit and the potential measuring circuit measure the cathode potential during energization, the energizing current value I and the cathode potential after energization interruption. Data from measuring device 7
Thus, the iron film resistance value Rf is obtained.
【0028】図2は上記計測装置7の一例のブロック図
である。FIG. 2 is a block diagram of an example of the measuring device 7.
【0029】図2において、8は演算および計測装置全
体の制御を行う中央処理部(CPU)、9は計測処理手
順、測定された陰極電位等の各種パラメータ、並びに予
め定められた基準値等を記憶する記憶部、10は複数点
入力される電位、電流のアナログ信号の切換器、11は
電位、電流のアナログ信号をデジタル信号に変換するア
ナログ→デジタル信号変換器、12は測定結果、操作指
令等を表示できる文字盤、13は計測装置に対し各種パ
ラメータ等をインプットするためのキーボード部、14
は測定を行う時等に用いるチャンネルセレクトスイッチ
部、15は測定結果あるいは設定パラメータの内容等を
用紙に印刷可能なプリンター部、16は計測装置に電力
を供給する電源部である。In FIG. 2, reference numeral 8 denotes a central processing unit (CPU) for performing arithmetic operations and control of the entire measuring apparatus, 9 denotes a measurement processing procedure, various parameters such as measured cathode potential, and predetermined reference values. A storage unit for storing, 10 is a switcher for an analog signal of electric potential and current input at a plurality of points, 11 is an analog-to-digital signal converter for converting an analog signal of electric potential and current into a digital signal, 12 is a measurement result, an operation command A dial that can display information such as a character, a keyboard portion 13 for inputting various parameters to the measuring device, and a reference numeral 14
Is a channel select switch unit used when performing measurement, 15 is a printer unit that can print the measurement result or the contents of setting parameters on paper, and 16 is a power supply unit that supplies power to the measuring device.
【0030】図3は自然電位Enおよび鉄皮膜抵抗値R
f から汚れおよび鉄皮膜の状態を同時に把握するための
概念図である。FIG. 3 shows the natural potential En and the iron film resistance value R.
It is a conceptual diagram for grasping the state of dirt and an iron film simultaneously from f.
【0031】スライム等による汚れが大きくなると自然
電位Enが貴になるという密接な関係がある。また、鉄
皮膜が厚く、耐食性が高くなると鉄皮膜抵抗値Rf が大
きくなるという密接な関係がある。従って、自然電位お
よび鉄皮膜抵抗値についてある基準値を予め定めると、
それらの値に基づいて図3に示すように鉄皮膜および汚
れの具合が把握される4つの区域(破線で区分されてい
る)に分けられる。There is a close relationship that the natural potential En becomes noble when the dirt due to slime or the like becomes large. Further, there is a close relation that the iron film resistance value Rf increases as the iron film becomes thicker and the corrosion resistance increases. Therefore, if a certain reference value is preset for the natural potential and the iron film resistance value,
Based on these values, as shown in FIG. 3, it is divided into four areas (divided by broken lines) in which the condition of the iron film and the dirt can be grasped.
【0032】従って、設備またはユニット毎に図3のよ
うな自然電位と鉄皮膜抵抗値との関係図を作成し、それ
らの目標基準値を予め定めておけば、実測した自然電位
および鉄皮膜抵抗値を同図中にプロットすることによっ
て対象とする設備の銅合金部材の汚れおよび鉄皮膜の状
態を同時にかつ容易に把握することが可能である。Therefore, if a relationship diagram between the natural potential and the iron film resistance value as shown in FIG. 3 is prepared for each facility or unit and the target reference values thereof are set in advance, the measured natural potential and the iron film resistance value are determined. By plotting the values in the figure, it is possible to easily and simultaneously grasp the state of the contamination and the iron film of the copper alloy member of the target equipment.
【0033】そして、鉄皮膜抵抗値が基準値以下であれ
ば鉄イオンを供給する等して鉄皮膜の強化を図り、また
自然電位が基準値より貴であればボール洗浄等によって
汚れを除去する指示を与えることが可能である。If the resistance of the iron film is below the reference value, iron ions are supplied to strengthen the iron film, and if the natural potential is nobler than the reference value, dirt is removed by ball cleaning or the like. It is possible to give instructions.
【0034】図4に本発明の銅合金部材の汚れの管理方
法を上記鉄皮膜抵抗の計測方法および真空度偏差値を利
用する方法と共に行なう際のフローの一例を示す。FIG. 4 shows an example of a flow for carrying out the method of controlling the contamination of the copper alloy member of the present invention together with the method of measuring the iron film resistance and the method of utilizing the vacuum degree deviation value.
【0035】図4において、En は自然電位(mV)、
Rf は鉄皮膜抵抗値(Ω・m2)、Rd は分極抵抗(Ω
・m2)、ΔHは真空度偏差値、tは入口水室温度
(℃)、グレードA洗浄はブラシ洗浄、グレードB洗浄
は硬質ボール洗浄、通常洗浄は軟質ボール洗浄をそれぞ
れ示す。In FIG. 4, En is the natural potential (mV),
Rf is the iron film resistance (Ω · m 2 ), Rd is the polarization resistance (Ω
M 2 ), ΔH is the degree of vacuum deviation, t is the inlet water chamber temperature (° C.), grade A cleaning is brush cleaning, grade B cleaning is hard ball cleaning, and normal cleaning is soft ball cleaning.
【0036】図4のフローに示すように、自然電位En
、鉄皮膜抵抗値Rf 、真空度偏差値ΔH等の測定、記
憶、演算、指令等が自動的に行なわれる。自然電位En
および鉄皮膜抵抗値Rf は対象設備の各ユニット毎に測
定され、それらの値を各々の基準値に基づく図3のよう
な概念図にプロットして該プロットの時間的推移を観察
することによって汚れ具合および鉄皮膜の状況が把握さ
れる。そして、上記概念図におけるプロットの位置、す
なわち汚れ具合および鉄皮膜の状況に応じてスライム等
の汚れ具合に基づく管内洗浄の要・不要、鉄イオン供給
装置の運転あるいは停止が各ユニット毎に判断され、設
備の運転を停止することなくリアルタイムに適格な指示
を行なうことができる。また、設備全体の汚れ具合を念
の為に真空度偏差値ΔHによっても管理しており、真空
度偏差値ΔHが基準値を超えた場合は設備全体を完全に
休止してブラシ洗浄することとしてある。なお、図4に
示した各基準値は実設備における一例を示したものであ
って、各設備または各ユニット毎に経験的に定められる
ものである。As shown in the flow chart of FIG. 4, the natural potential En
, The iron film resistance value Rf, the vacuum deviation value ΔH, etc. are automatically measured, stored, calculated, commanded and the like. Natural potential En
And the iron film resistance value Rf are measured for each unit of the target equipment, and those values are plotted on a conceptual diagram based on the respective reference values as shown in FIG. 3 and the time transition of the plot is observed to observe the contamination. The condition and the condition of the iron film are grasped. Then, depending on the position of the plot in the above conceptual diagram, that is, the degree of contamination and the state of the iron film, it is determined for each unit whether or not to clean the inside of the pipe based on the degree of contamination such as slime and the operation or stop of the iron ion supply device. , It is possible to give qualified instructions in real time without stopping the operation of the equipment. In addition, the vacuum degree deviation value ΔH is also used to control the degree of contamination of the entire equipment, and if the vacuum degree deviation value ΔH exceeds the reference value, the entire equipment is completely stopped and brush cleaning is performed. is there. The reference values shown in FIG. 4 are examples of actual equipment and are empirically determined for each equipment or each unit.
【0037】[0037]
【実施例】以下、実施例に基づいて本発明をより詳細に
説明するが、これによって本発明の管理方法が限定され
るものではない。The present invention will be described in more detail based on the following examples, but the present invention is not limited thereto.
【0038】実施例 外部電源方式による電気防食装置と鉄電解法による鉄イ
オン供給装置を設けた火力発電所の復水器の1ユニット
について本発明の管理方法を適用した。なお、本実施例
においてはそのユニットだけの真空度偏差値ΔHを測定
するため、他のユニットは閉鎖して行なった。対象とす
る復水器は海水を冷却水として用いており、アルミニウ
ム黄銅冷却管とネーバル黄銅管板とを具備するものであ
る。[0038] applying the management method of the present invention for one unit of Embodiment external power supply method sacrificial apparatus and condenser thermal power plant provided with an iron ion supply device according to the iron electrolysis by. In this example, the vacuum degree deviation value ΔH of only that unit was measured, so that the other units were closed. The target condenser uses seawater as cooling water, and is equipped with an aluminum brass cooling pipe and a Naval brass tube plate.
【0039】(基準値の設定)先ず、対象となる復水器
における自然電位Enおよび鉄皮膜抵抗値Rf の各々の
基準値を求めるための事前調査を行なった。(Setting of Reference Value) First, a preliminary investigation was carried out for obtaining the reference values of the natural potential En and the iron film resistance value Rf of the subject condenser.
【0040】電気防食および鉄イオン供給を6ヶ月行な
って生物やマンガンスケール等のスライム付着物が蓄積
した復水器の管内をジェット洗浄した。その後、電気防
食および鉄イオン供給を再開し、約3ヶ月間に亘って管
内付着物を定期的に採集して付着物量を測定した。ま
た、採集と同時に前述の計測装置を用いて自然電位E
n、鉄皮膜抵抗値Rf および真空度偏差値ΔHを測定し
た。The interior of the condenser pipe in which organisms and slime deposits such as manganese scale were accumulated was jet-cleaned by performing cathodic protection and supplying iron ions for 6 months. After that, the cathodic protection and the iron ion supply were restarted, and the deposits in the tube were periodically collected for about 3 months to measure the deposit amount. At the same time as the collection, the self-potential E
n, the iron film resistance value Rf and the vacuum degree deviation value ΔH were measured.
【0041】なお、自然電位En は飽和甘汞電極(SC
E)基準で前記式(1)に基づいて求めたが、表1から
明らかなように、その値は実測した自然電位(通電遮断
後5分後の陰極電位)と充分に一致するものであった。The natural potential En is the saturated sweet potato electrode (SC
E) Based on the above equation (1) on the basis of the reference, as is clear from Table 1, the value is sufficiently coincident with the measured natural potential (cathode potential 5 minutes after the interruption of energization). It was
【0042】[0042]
【表1】 。[Table 1] .
【0043】図5に付着物量と自然電位En および鉄皮
膜抵抗値Rf との関係を示したグラフ、図6に付着物量
と真空度偏差値ΔHとの関係を示したグラフ、図7に真
空度偏差値ΔHと自然電位En および鉄皮膜抵抗値Rf
との関係を示したグラフをそれぞれ示す。FIG. 5 is a graph showing the relationship between the amount of deposits, the natural potential En and the iron film resistance value Rf, FIG. 6 is a graph showing the relationship between the amount of deposits and the vacuum deviation ΔH, and FIG. 7 is the vacuum degree. Deviation ΔH, spontaneous potential En and iron film resistance Rf
The graphs showing the relationship with are respectively shown.
【0044】図5から明らかなように、自然電位En は
付着物量と密接な関係があり、管内付着物量(生物やマ
ンガンスケール等のスライム量)の増加に伴って自然電
位En は貴化し、他方鉄皮膜抵抗値Rf は低下してい
る。As is clear from FIG. 5, the natural potential En has a close relationship with the amount of deposits, and as the amount of deposits in the tube (the amount of slime such as organisms and manganese scale) increases, the spontaneous potential En becomes more noble. The iron film resistance value Rf is decreasing.
【0045】また、真空度偏差値ΔHは従来から実際の
操業において設備全体の汚れの具合を把握するための指
標として広く使用されており、図6に示すように付着物
量と密接な関係がある(但し、複数のユニットを具備す
る通常の設備にあっては付着物量は全ユニットで均一で
はないので、各ユニット毎に汚れの具合を把握すること
はできない)。Further, the vacuum degree deviation value ΔH has been widely used as an index for grasping the degree of contamination of the entire equipment in actual operation, and is closely related to the amount of deposits as shown in FIG. (However, since the amount of deposits is not uniform in all units in ordinary equipment that includes multiple units, it is not possible to determine the degree of contamination for each unit).
【0046】そこで、本実施例においては真空度偏差値
ΔHを参考にして自然電位En および鉄皮膜抵抗値Rf
の基準値を定める。すなわち、従来、真空度偏差値ΔH
が2〜3mmHgになるとボール洗浄を行なうことが好まし
かった場合、例えば真空度偏差値ΔH=3mmHgを基準と
する。そして、その値に対応する付着物量は図6から
4.5mg/cm2である。従って、付着物量を4.5mg/
cm2以下に管理するためには図5から自然電位En の基
準値を−150mV(SCE)に定めればよいことが分
かる。また、鉄皮膜抵抗値Rf はそれに対応する0.6
5Ω・m2とすればよい。Therefore, in this embodiment, the spontaneous potential En and the iron film resistance value Rf are referred to with reference to the vacuum degree deviation value ΔH.
Determine the standard value of. That is, conventionally, the degree of vacuum deviation ΔH
When it is preferable to perform ball cleaning when the value becomes 2 to 3 mmHg, the vacuum degree deviation value ΔH = 3 mmHg is used as a reference. The amount of deposits corresponding to that value is 4.5 mg / cm 2 from FIG. Therefore, the amount of deposit is 4.5 mg /
It can be seen from FIG. 5 that the reference value of the natural potential En can be set to −150 mV (SCE) in order to control the value to be cm 2 or less. The iron film resistance value Rf is 0.6
It may be 5 Ω · m 2 .
【0047】また、図7に示す真空度偏差値ΔHと自然
電位En および鉄皮膜抵抗値Rf との関係に基づいて、
真空度偏差値ΔHから直接各基準値を定めてもよい。Further, based on the relationship between the vacuum degree deviation value ΔH, the natural potential En and the iron film resistance value Rf shown in FIG.
Each reference value may be determined directly from the vacuum degree deviation value ΔH.
【0048】このように各基準値を設定すると、図5か
ら明らかなように、自然電位En が−150mVより貴
になる程汚れが顕著(付着物量が4.5mg/cm2超)で
熱貫流効率の低下を招き、また鉄皮膜抵抗値Rf が0.
65Ω・m2以下になると鉄皮膜の防食効果がスライム
付着による汚れの蓄積で低下していることが把握できる
ので、ボール洗浄等で管内を洗浄する警報の告知基準と
なる。When the respective reference values are set in this way, as is apparent from FIG. 5, as the spontaneous potential En becomes nobler than -150 mV, the contamination becomes remarkable (the amount of deposits is more than 4.5 mg / cm 2 ) and the heat flow-through occurs. This leads to a decrease in efficiency, and the iron film resistance value Rf is less than 0.
When it is less than 65 Ω · m 2 , it can be understood that the anticorrosion effect of the iron film is reduced due to the accumulation of dirt due to slime adhesion, so it becomes a warning notification standard for cleaning the inside of the pipe by ball cleaning or the like.
【0049】従って、上記の各基準値に基づいて、自然
電位Enおよび鉄皮膜抵抗値Rf から汚れおよび鉄皮膜
の状態を同時に把握することができる概念図が得られる
(図8)。そして、自然電位および鉄皮膜抵抗値の実測
値を同図中にプロットすることによって対象とする部材
の汚れおよび鉄皮膜の状態を同時にかつ容易に把握する
ことができ、適切な対応をリアルタイムにとることがで
きる。Therefore, based on each of the above reference values, a conceptual diagram can be obtained in which the states of the dirt and the iron film can be grasped at the same time from the natural potential En and the iron film resistance value Rf (FIG. 8). Then, by plotting the measured values of the self-potential and the resistance value of the iron film in the figure, it is possible to easily and simultaneously grasp the stains on the target member and the state of the iron film, and take appropriate action in real time. be able to.
【0050】なお、管理をより厳しくする場合は、例え
ば真空度偏差値ΔH=2mmHgを基準としてその値に対応
する自然電位En =−200mVおよび鉄皮膜抵抗値R
f =0.7Ω・m2を基準値とすればよい。In the case where the control is made more strict, for example, with reference to the vacuum deviation value ΔH = 2 mmHg, the natural potential En = −200 mV and the iron film resistance value R corresponding to that value are used.
The reference value may be f = 0.7Ω · m 2 .
【0051】(復水器の運転管理)次に、上記の基準値
を用いて実際に復水器の運転管理を行なった。(Operation Management of Condenser) Next, the operation management of the condenser was actually performed using the above-mentioned reference value.
【0052】復水器の管内をジェット洗浄して内面を清
浄にした状態から電気防食および鉄イオン供給を開始
し、前述の計測装置を用いて自然電位En 、鉄皮膜抵抗
値Rfおよび真空度偏差値ΔHを約4ヶ月間測定した。From the state in which the inside of the condenser pipe was jet-cleaned to clean the inner surface, the electrocorrosion and the iron ion supply were started, and the self-potential En, the iron film resistance value Rf, and the vacuum degree deviation were measured using the above-mentioned measuring device. The value ΔH was measured for about 4 months.
【0053】自然電位En および鉄皮膜抵抗値Rf の実
測値を図8にプロットして得たグラフを図9に示す。図
9中、黒丸(・)は実測値を示し、矢線(→)は測定お
よび復水器稼働開始後の時間の経過を示す。なお、測定
開始は晩春であり、スライムの生成しやすい夏期を経て
初秋までの記録である。A graph obtained by plotting the measured values of the natural potential En and the iron film resistance value Rf in FIG. 8 is shown in FIG. In FIG. 9, black circles (•) indicate measured values, and arrow lines (→) indicate elapsed time after the start of measurement and operation of the condenser. It should be noted that the measurement was started in the late spring, and it is a record from the summer when the slime is easily generated to the early autumn.
【0054】図9における測定値を経時的に見ると、測
定値は帯状となって移行しており、大きく4ブロックに
分けられる。すなわち、測定開始直後(晩春)は管内面
は清浄で、自然電位En は約−400mVでかつ鉄皮膜
抵抗値Rf が0.65Ω・m2以下であることから、電
気防食による防食効果が有効に働いていることが把握で
きる。この間鉄イオンの供給も同時に行なっているので
時間の経過と共に鉄皮膜抵抗値Rf は増大している。ま
た、鉄皮膜の形成に伴って徐々に自然電位Enが貴化し
ているが、この時期は電気防食による防食効果が支配的
である。When the measured values in FIG. 9 are viewed with time, the measured values are band-shaped and shifted, and can be roughly divided into 4 blocks. That is, immediately after the start of measurement (late spring), the inner surface of the tube was clean, the spontaneous potential En was about -400 mV, and the iron film resistance value Rf was 0.65 Ω · m 2 or less, so the anticorrosion effect due to galvanic protection was effective. You can understand that you are working. During this period, iron ions are also supplied at the same time, so that the iron film resistance value Rf increases with the passage of time. Further, the spontaneous potential En gradually becomes noble with the formation of the iron film, but at this time, the anticorrosion effect by the electrocorrosion is dominant.
【0055】初夏になると鉄皮膜抵抗値Rf は急速に増
大し、自然電位En も貴化が進んでいることから、形成
された鉄皮膜が固まり、さらにスライムの付着が始まっ
たことが把握できる。この時期は電気防食による防食か
ら鉄皮膜による防食に次第に移行していることが分か
る。In early summer, the resistance value Rf of the iron film rapidly increases, and the spontaneous potential En is also becoming more noble. Therefore, it can be understood that the formed iron film is solidified and the adhesion of slime is started. It can be seen that during this period, the corrosion protection by the electrolytic protection gradually shifts to the corrosion protection by the iron film.
【0056】夏期になると自然電位En の貴化が著し
く、鉄皮膜抵抗値Rf はピーク値から急速に低下してい
ることから、スライムの生成が盛んで、汚れが顕著にな
っていることが把握できる。この期間の終りには鉄皮膜
抵抗値Rf は0.65Ω・m2以下となり、かつ自然電
位En も−150mVより貴化したので、図4のフロー
に従ってボール洗浄(軟質)を実施した。なお、上記期
間の終りには真空度偏差値ΔHも3mmHgを超えていた。In the summer, the spontaneous potential En is remarkably noble and the iron film resistance value Rf is rapidly decreased from the peak value. Therefore, it is understood that the slime is prominent and the contamination is remarkable. it can. At the end of this period, the iron film resistance value Rf became 0.65 Ω · m 2 or less, and the natural potential En also became noble from -150 mV, so ball cleaning (softening) was carried out according to the flow of FIG. At the end of the above period, the vacuum degree deviation value ΔH also exceeded 3 mmHg.
【0057】ボール洗浄を行なった結果、晩夏には自然
電位En および鉄皮膜抵抗値Rf が初夏の時期と略同様
まで回復し(図中斜線部)、汚れおよび鉄皮膜が良好な
状態に回復したことが把握できる。As a result of ball cleaning, in the late summer, the spontaneous potential En and the resistance value Rf of the iron film were restored to almost the same level as in the early summer (hatched portion in the figure), and the dirt and the iron film were restored to a good state. I can understand.
【0058】以下に、上記測定期間における真空度偏差
値ΔHと冷却管内の鉄皮膜および汚れ具合とを表2に示
す。Table 2 shows the vacuum deviation ΔH, the iron film in the cooling pipe, and the degree of contamination during the above measurement period.
【0059】[0059]
【表2】 。[Table 2] .
【0060】表2から明らかなように、本発明の汚れの
管理方法と前記鉄皮膜抵抗の計測方法とを併せて行なっ
て自然電位Enおよび鉄皮膜抵抗値Rf から汚れおよび
鉄皮膜の状態を把握した結果は、従来から行なわれてい
る真空度偏差値ΔH並びに冷却管内の鉄皮膜および汚れ
具合とよく対応しており、特に汚れ具合が適格に把握さ
れていることが分かる。As is clear from Table 2, the state of the dirt and the iron film is grasped from the spontaneous potential En and the iron film resistance value Rf by performing the dirt management method of the present invention and the iron film resistance measuring method together. The obtained results correspond well with the conventionally used vacuum degree deviation value ΔH and the iron film in the cooling pipe and the degree of contamination, and it is understood that the degree of contamination is particularly well understood.
【0061】さらに、本発明の汚れの管理方法に従って
洗浄を行なったところ、汚れおよび鉄皮膜が良好な状態
に回復したことから、本発明の方法が有効であることが
分かる。Furthermore, when the cleaning was carried out according to the method for controlling dirt of the present invention, the dirt and the iron film were recovered to a good state, which shows that the method of the present invention is effective.
【0062】[0062]
【発明の効果】以上説明した如く、本発明の管理方法に
よって、海水等を冷却水として使用する復水器、熱交換
器等の設備における冷却管、管板等の銅合金部材の表面
に形成するスライム等の汚れ具合をリアルタイムに把握
することが可能となる。そして、その汚れを管理するこ
とによって鉄皮膜の防食効果の低下および設備の熱貫流
効率の低下をユニット毎に防止でき、設備を効率的に適
正稼働状態に維持することが可能となる。As described above, according to the management method of the present invention, it is formed on the surface of a copper alloy member such as a cooling pipe or a tube plate in a condenser such as a condenser or a heat exchanger that uses seawater as cooling water. It becomes possible to grasp in real time how dirty the slime is. Then, by controlling the contamination, it is possible to prevent the deterioration of the anticorrosion effect of the iron film and the reduction of the heat transmission efficiency of the equipment for each unit, and it is possible to efficiently maintain the equipment in an appropriate operating state.
【0063】また、本発明に係る自然電位は複数のユニ
ットからなる復水器、熱交換器等の設備においてユニッ
ト毎に測定できるので、本発明によればユニット毎にそ
の汚れの状態を把握することが可能となり、設備をユニ
ット毎に非常に効率的に管理することができる。Since the self-potential according to the present invention can be measured for each unit in equipment such as a condenser, heat exchanger, etc., which comprises a plurality of units, according to the present invention, the state of contamination can be grasped for each unit. Therefore, the equipment can be managed very efficiently for each unit.
【0064】さらに、本発明の汚れの管理方法は鉄皮膜
抵抗の計測方法と併せて行なうことができ、そうするこ
とによって汚れの管理と鉄皮膜の状態とを同一の装置で
しかも同時に把握することが可能となり、設備をより効
率的に適正稼働状態に維持することが可能である。Furthermore, the method for controlling dirt of the present invention can be carried out together with the method for measuring the resistance of the iron film, and by doing so, the management of dirt and the state of the iron film can be grasped simultaneously by the same device. It becomes possible to maintain the equipment in a proper operating state more efficiently.
【0065】従って、本発明によれば設備のトラブルは
未然に防止でき、万一異常が生じた場合にも直ちに処理
ができるので、設備を常に安全かつ効率的に操業するこ
とが可能となる。Therefore, according to the present invention, the trouble of the equipment can be prevented in advance, and the processing can be immediately performed even if an abnormality should occur, so that the equipment can always be operated safely and efficiently.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の管理方法を実施するための通電装置の
一例のブロック図である。FIG. 1 is a block diagram of an example of a power supply device for implementing a management method of the present invention.
【図2】計測装置7の一例のブロック図である。FIG. 2 is a block diagram of an example of a measuring device 7.
【図3】自然電位および鉄皮膜抵抗値から汚れおよび鉄
皮膜の状態を同時に把握するための概念図である。FIG. 3 is a conceptual diagram for simultaneously grasping the states of dirt and an iron film from the natural potential and the resistance value of the iron film.
【図4】本発明の銅合金部材の汚れの管理方法を上記鉄
皮膜抵抗の計測方法および真空度偏差値を利用する方法
と共に行なう際のフローの一例である。FIG. 4 is an example of a flow for performing the method for controlling the contamination of the copper alloy member of the present invention together with the method for measuring the iron film resistance and the method for utilizing the vacuum deviation value.
【図5】付着物量と自然電位En および鉄皮膜抵抗値R
f との関係を示したグラフである。FIG. 5: Amount of deposit, natural potential En and iron film resistance value R
It is a graph showing the relationship with f.
【図6】付着物量と真空度偏差値ΔHとの関係を示した
グラフである。FIG. 6 is a graph showing the relationship between the amount of deposits and the vacuum degree deviation value ΔH.
【図7】真空度偏差値ΔHと自然電位En および鉄皮膜
抵抗値Rf との関係を示したグラフである。FIG. 7 is a graph showing the relationship between the vacuum deviation value ΔH, the natural potential En, and the iron film resistance value Rf.
【図8】自然電位および鉄皮膜抵抗値から汚れおよび鉄
皮膜の状態を同時に把握するための概念図である。FIG. 8 is a conceptual diagram for simultaneously grasping the states of dirt and iron film from the natural potential and the resistance value of the iron film.
【図9】自然電位および鉄皮膜抵抗値の実測値を図8に
プロットしたグラフである。FIG. 9 is a graph in which the measured values of the natural potential and the resistance value of the iron film are plotted in FIG.
1 通電用電極 2 管板面 3 冷却管 4 基準電極 5 水室 6 直流電源装置 7 計測装置 A 電流測定回路 E 電位測定回路 1 energizing electrode 2 tube plate surface 3 cooling tube 4 reference electrode 5 water chamber 6 DC power supply device 7 measuring device A current measuring circuit E potential measuring circuit
───────────────────────────────────────────────────── フロントページの続き (72)発明者 蜂谷 実 千葉県船橋市藤原町1−172−8 (56)参考文献 特開 昭59−147247(JP,A) 特開 平1−139998(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Minoru Hachiya 1-172-8 Fujiwara, Funabashi City, Chiba (56) References JP-A-59-147247 (JP, A) JP-A-1-139998 (JP, A)
Claims (5)
合金部材を電気防食法と該部材の表面に鉄皮膜を形成さ
せることによる防食法とを併用して防食する際における
該銅合金部材の汚れの管理において、該冷却水中に設け
た電極から該冷却水を通じて該銅合金部材に通電する電
流回路と、該銅合金部材の電位を測定する電位測定回路
とを有する通電装置を用いて、該通電を一時的に遮断し
た後に陰極(銅合金部材)電位が減衰して安定するとこ
ろの自然電位を求める工程と、該自然電位を予め定めら
れた基準値と比較する工程と、該自然電位が該基準値よ
り貴になると該銅合金部材の汚れを洗浄する工程とから
なることを特徴とする、銅合金部材の汚れの管理方法。1. A copper alloy used for corrosion protection of a copper alloy member used in equipment requiring cooling water, using both an anticorrosion method and a corrosion prevention method by forming an iron film on the surface of the member. In controlling the contamination of a member, using a current-carrying device having a current circuit for supplying current to the copper alloy member from the electrode provided in the cooling water through the cooling water, and a potential measuring circuit for measuring the potential of the copper alloy member. , A step of obtaining a natural potential where the potential of the cathode (copper alloy member) is attenuated and stabilized after the current is temporarily cut off, a step of comparing the natural potential with a predetermined reference value, A method for controlling contamination of a copper alloy member, which comprises a step of cleaning the contamination of the copper alloy member when the potential becomes nobler than the reference value.
を遮断してから50秒後の陰極電位(mV)、E60は
通電を遮断してから60秒後の陰極電位(mV)をそれ
ぞれ示す]に基づいて求めることを特徴とする、請求項
1に記載の銅合金部材の汚れの管理方法。2. The natural potential is expressed by the following formula (1) En = E 60 + (E 60 −E 50 ) (1) [In the formula (1), En is a natural potential (mV) and E 50 is a current. The cathode potential (mV) 50 seconds after the interruption, E 60 represents the cathode potential (mV) 60 seconds after the interruption of the energization, respectively]. A method for controlling contamination of a copper alloy member as described.
ル洗浄、硬質ボール洗浄およびジェット洗浄よりなる群
から選ばれる少なくとも一種の洗浄方法によって行なう
ことを特徴とする、請求項1または2に記載の銅合金部
材の汚れの管理方法。3. The cleaning method according to claim 1, wherein the step of cleaning the dirt is performed by at least one cleaning method selected from the group consisting of soft ball cleaning, hard ball cleaning and jet cleaning. For controlling the contamination of copper alloy parts of.
低下および/または前記設備の熱貫流効率の低下が許容
範囲を超えないように経験的に定めることを特徴とす
る、請求項1〜3のうちのいずれかに記載の銅合金部材
の汚れの管理方法。4. The reference value is empirically determined such that a reduction in the anticorrosion effect of the iron coating and / or a reduction in the heat transmission efficiency of the equipment does not exceed an allowable range. 4. A method for controlling contamination of a copper alloy member according to any one of 3 to 3.
防食装置であることを特徴とする、請求項1〜4のうち
のいずれかに記載の銅合金部材の汚れの管理方法。5. The method for controlling contamination of a copper alloy member according to claim 1, wherein the energizing device is an external power source type anticorrosion device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3063665A JPH07117355B2 (en) | 1991-03-06 | 1991-03-06 | How to control dirt on copper alloy parts |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3063665A JPH07117355B2 (en) | 1991-03-06 | 1991-03-06 | How to control dirt on copper alloy parts |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04278198A JPH04278198A (en) | 1992-10-02 |
| JPH07117355B2 true JPH07117355B2 (en) | 1995-12-18 |
Family
ID=13235868
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3063665A Expired - Fee Related JPH07117355B2 (en) | 1991-03-06 | 1991-03-06 | How to control dirt on copper alloy parts |
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| Country | Link |
|---|---|
| JP (1) | JPH07117355B2 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4873919B2 (en) * | 2005-10-07 | 2012-02-08 | 中国電力株式会社 | Iron ion implantation method and iron ion implantation amount control device |
| JP4964066B2 (en) * | 2007-09-06 | 2012-06-27 | 中部電力株式会社 | Countermeasure against heat exchanger scale |
| JP6015358B2 (en) * | 2012-11-01 | 2016-10-26 | 栗田エンジニアリング株式会社 | Corrosion prevention method for copper alloy heat exchangers |
| JP2017156025A (en) * | 2016-03-02 | 2017-09-07 | 東京電力ホールディングス株式会社 | Heat exchange system |
-
1991
- 1991-03-06 JP JP3063665A patent/JPH07117355B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04278198A (en) | 1992-10-02 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |