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JPS5844200B2 - Corrosion prevention method for heat exchangers - Google Patents
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JPS5844200B2 - Corrosion prevention method for heat exchangers - Google Patents

Corrosion prevention method for heat exchangers

Info

Publication number
JPS5844200B2
JPS5844200B2 JP53096353A JP9635378A JPS5844200B2 JP S5844200 B2 JPS5844200 B2 JP S5844200B2 JP 53096353 A JP53096353 A JP 53096353A JP 9635378 A JP9635378 A JP 9635378A JP S5844200 B2 JPS5844200 B2 JP S5844200B2
Authority
JP
Japan
Prior art keywords
corrosion
iron
electrode
film
ion generator
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
Application number
JP53096353A
Other languages
Japanese (ja)
Other versions
JPS5523857A (en
Inventor
清美 斉藤
隆 池沢
教正 兵藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Tokyo Shibaura Electric Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP53096353A priority Critical patent/JPS5844200B2/en
Publication of JPS5523857A publication Critical patent/JPS5523857A/en
Publication of JPS5844200B2 publication Critical patent/JPS5844200B2/en
Expired legal-status Critical Current

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  • Prevention Of Electric Corrosion (AREA)

Description

【発明の詳細な説明】 この発明は冷却水として海水を使用する発電用大型復水
器などの銅合金系チューブを用いる熱交換器の防食方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing corrosion of heat exchangers using copper alloy tubes, such as large condensers for power generation that use seawater as cooling water.

一般に銅合金系部材の耐食性は表面に形成される防食皮
膜に左右され、その中でも特に耐食性能の向上に重要な
役割をもつものが鉄系の防食皮膜であることが広く知ら
れている。
In general, the corrosion resistance of copper alloy-based members depends on the anti-corrosion coating formed on the surface, and it is widely known that iron-based anti-corrosion coatings play a particularly important role in improving corrosion resistance.

この鉄系の防食皮膜の形成は主として冷却水中に含まれ
る第1鉄イオンの濃度に左右されることから従来、熱交
換器の銅合金系チューブを防食する場合は冷却水系内に
硫酸第1鉄を注入混合することにより鉄イオンを供給し
てチューブ内壁に防食性酸化鉄皮膜を形成する方法が行
なわれ、またこの方法に不溶性電極による電気防食法を
組み合わせることが多く行なわれていたが、硫酸第1鉄
は吸湿性の粉末のために保存や取り扱いなどの薬品管理
が繁雑なことや溶解注入作業などに多くの人員と時間を
必要とすること、および冷却水を茶褐色に変色させるな
どの問題があることから省力化および環境保全の観点か
ら新防食方式の開発が望まれていた。
The formation of this iron-based anti-corrosion film mainly depends on the concentration of ferrous ions contained in the cooling water. A method of supplying iron ions by injecting and mixing sulfuric acid to form an anticorrosive iron oxide film on the inner wall of the tube was used, and this method was often combined with cathodic protection using an insoluble electrode. Since ferrous iron is a hygroscopic powder, chemical management such as storage and handling is complicated, many people and time are required for dissolution and injection work, and there are problems such as discoloration of cooling water to brown. Therefore, the development of a new anti-corrosion method was desired from the viewpoint of labor saving and environmental protection.

このため、鉄イオンの供給を電解方式とするための研究
開発が行なわれ、取水路中に大型電解式鉄イオン発生装
置を設置する方式←持開昭5244742号)や、電気
防食用電極として溶解性鉄電極を用いる方式(実開昭5
2−76523号)などの鉄イオン供給技術が開発され
てきた。
For this reason, research and development was carried out to supply iron ions using an electrolytic method, including a method of installing a large electrolytic iron ion generator in the intake channel (No. 5244742), and a method of dissolving iron ions as electrodes for cathodic protection. A method using iron electrodes (1986)
Iron ion supply technologies such as No. 2-76523) have been developed.

しかしながら、前者の方式は防食皮膜を形成するために
十分な鉄イオンを供給することができるが、装置が大型
で電力消費量が多くなること、また後者の方式は装置が
小型で電力消費量が少ないが、鉄イオン供給量が十分で
ない場合があるなどの難点があり、さらに技術開発が求
められていた。
However, although the former method can supply sufficient iron ions to form an anti-corrosion film, the equipment is large and consumes a lot of power, while the latter method has a small equipment and consumes a lot of power. Although the amount of iron ions supplied is small, there are some drawbacks such as insufficient supply of iron ions, and further technological development is required.

本発明者らは、このような問題に対し銅合金系チューブ
の防食皮膜の形成および維持と鉄イオン供給量との関係
に着眼し、従来から蓄積した技術や経験をもとに鋭意研
究した結果、冷却水中の鉄イオン濃度と防食皮膜形成と
に密接な関係のあることが判明されてきた。
The inventors of the present invention focused on the relationship between the formation and maintenance of the anticorrosion coating on copper alloy tubes and the amount of iron ion supplied, and as a result of intensive research based on the technology and experience accumulated over the years. It has been found that there is a close relationship between the iron ion concentration in cooling water and the formation of an anticorrosive film.

すなわち、初期皮膜形成時には0.1〜0.5 ppm
の、破壊皮膜再生時には0.01〜0.03ppmの、
また完成皮膜維持には0.001〜0.01ppmの鉄
イオン濃度とするのが、皮膜の形成および維持において
好ましいことが解明された。
That is, 0.1 to 0.5 ppm during initial film formation.
, 0.01 to 0.03 ppm when regenerating the destroyed film.
It has also been found that an iron ion concentration of 0.001 to 0.01 ppm is preferable for forming and maintaining a completed film.

このことは、防食皮膜の形成維持において、初期には大
量の、維持には小量の、皮膜状態によって再生用の中量
の鉄イオンを必要とするから、これらに応じた鉄イオン
の供給システムを開発すれば良いことになる。
This means that to maintain the formation of a corrosion-resistant film, a large amount of iron ions is required initially, a small amount for maintenance, and a medium amount for regeneration depending on the state of the film, so the iron ion supply system must be adjusted accordingly. It would be a good idea to develop

以上のような研究成果から、本発明者らは、熱交換器の
銅合金系チューブの防食皮膜の形成および維持において
、冷却水取水路に鉄イオンを供給する電解式鉄イオン発
生装置と、熱交換器の水入口側水室内に電気防食用電極
として溶解性鉄電極を設け、チューブ防食皮膜の形成状
態に応じて電解式鉄イオン発生装置を動作させ安定防食
皮膜を形成させると共に、溶解性鉄電極を用いた電気防
食によって防食皮膜を維持させるための鉄イオンを供給
することが前述の条件を満足させる有効な鉄イオンの供
給システムであることを見い出すに至った。
Based on the above research results, the present inventors have developed an electrolytic iron ion generator that supplies iron ions to the cooling water intake channel and a thermal A soluble iron electrode is installed as an electrode for cathodic protection in the water chamber on the water inlet side of the exchanger, and an electrolytic iron ion generator is operated according to the formation status of the tube anticorrosion coating to form a stable anticorrosion coating, and at the same time It has been discovered that supplying iron ions to maintain the anticorrosive film by electrolytic protection using electrodes is an effective iron ion supply system that satisfies the above conditions.

しかしながら、このように鉄イオン濃度で防食皮膜を管
理する方法は、冷却水の流量の変化に対応することがで
きないために、鉄イオンが厚く付着してチューブの伝熱
効率を低下させたり、鉄イオン付着量の不足によってチ
ューブの防食が損われたりするおそれがあり十分なもの
ではなかった。
However, this method of controlling the anti-corrosion film based on iron ion concentration cannot respond to changes in the flow rate of cooling water, so iron ions may adhere thickly and reduce the heat transfer efficiency of the tube, or iron ions may This was not sufficient as there was a risk that the corrosion protection of the tube would be impaired due to insufficient adhesion.

このようなことから、銅合金系チューブの防食管理では
、その防食状況が明確に確認でき、これを基にして適正
な鉄イオンの供給を継続させる手段が必要であることが
わかった。
From these facts, it has been found that in the corrosion protection management of copper alloy tubes, it is necessary to have a means to clearly check the corrosion protection status and to continue to supply an appropriate amount of iron ions based on this.

従来、鉄イオン供給法における防食状況の確認はで定時
間鉄イオンを供給した後に冷却管を引き抜きその一部を
切り取るか、あらかじめ水室内に設置した試料片を取り
出して表面に形成された防食保護皮膜の状態を観察しそ
の成分を分析するなどの方法によるため、その判断には
時間的な制約をうけるとともに多大の手間ひまを必要と
していた。
Conventionally, the corrosion protection status in the iron ion supply method was confirmed by supplying iron ions for a fixed period of time, then pulling out the cooling tube and cutting a part of it, or by taking out a sample piece that had been placed in a water chamber in advance and checking the corrosion protection formed on the surface. Since this method involves observing the state of the film and analyzing its components, the determination is subject to time constraints and requires a great deal of time and effort.

本発明者らは、長年にわたって蓄積されたデータを基に
して、銅合金部材表面に形成される防食保護皮膜の陰分
極抵抗値と皮膜状態との間に下表のような密接な関係が
あることを見い出した。
Based on data accumulated over many years, the present inventors have found that there is a close relationship between the cathodic polarization resistance value of the anti-corrosion protective film formed on the surface of the copper alloy member and the state of the film, as shown in the table below. I discovered that.

本発明はこのような事実に基づき、銅合金系チューブの
防食皮膜の状態を陰分極抵抗方式、例えば水室内に設け
た電気防食装置を利用して陰分極抵抗値を計測し、この
分極抵抗値をもとに電気防食の防食電流と電解式鉄イオ
ン発生装置とを自動的に制御し、防食電流と鉄イオン供
給量とを適正値に設置することによって、熱交換器の防
食状況を適格かつ合理的に管理するものである。
Based on these facts, the present invention measures the state of the anti-corrosion coating on copper alloy tubes using a cathodic polarization resistance method, for example, using a cathodic protection device installed in a water chamber, and calculates the polarization resistance value. By automatically controlling the corrosion protection current for cathodic protection and the electrolytic iron ion generator based on the It shall be managed rationally.

つぎに、本発明防食法の実施例を図面によって具体的に
説明する。
Next, embodiments of the anticorrosion method of the present invention will be specifically described with reference to the drawings.

図面は発電用プラントの復水器に本発明の方法を実施す
る場合の平面図で、冷却水取水路1中に設置した電解式
鉄イオン発生装置2により、復水器3中の銅合金系チュ
ーブの防食皮膜の初期形成および再生用鉄イオンの供給
を行なう。
The drawing is a plan view of the case where the method of the present invention is applied to a condenser of a power generation plant. Initial formation of anti-corrosion coating on the tube and supply of iron ions for regeneration.

一方、復水器3の水室内に設置した電気防食用鉄電極4
からは、防食電流の通電と防食皮膜の維持に必要な鉄イ
オンの供給を行なう。
On the other hand, an iron electrode 4 for cathodic protection installed in the water chamber of the condenser 3
From this point, an anti-corrosion current is applied and iron ions necessary for maintaining the anti-corrosion film are supplied.

電解式鉄イオン発生装置2は電源装置5によって直流電
流の供給と制御がなされ、溶出鉄イオン量が管理される
The electrolytic iron ion generator 2 is supplied with DC current and controlled by a power supply device 5, and the amount of eluted iron ions is managed.

また、鉄電極装置4は電気防食用電源装置6によって直
流電流の供給と制御がなされ、鉄イオンの溶出量と防食
電流量が管理される。
Further, direct current is supplied and controlled to the iron electrode device 4 by a cathodic protection power supply device 6, and the elution amount of iron ions and the amount of corrosion protection current are managed.

7は復水器3の水室内に設けられた陰分極抵抗計副極で
あり、これによって銅合金系チューブの電位を測定し、
このデータを演算処理回路8に入力して陰分極抵抗値を
求めるとともに、この値によりチューブの防食皮膜状態
を判断することによって電気防食用出力電流および電解
式鉄イオン発生装置出力電流の適正値の計算を行ない、
それぞれの装置に制御信号を送り防食電流と鉄イオン供
給量を自動的に制御する。
7 is a sub-electrode of a cathode polarization resistance meter installed in the water chamber of the condenser 3, which measures the potential of the copper alloy tube.
This data is input to the arithmetic processing circuit 8 to determine the cathodic polarization resistance value, and this value is used to judge the state of the anticorrosion coating on the tube, thereby determining the appropriate value of the output current for cathodic protection and the output current of the electrolytic iron ion generator. do the calculations,
Control signals are sent to each device to automatically control the corrosion protection current and iron ion supply amount.

なお、本実施例では陰分極抵抗計副極1は電気防食用電
位計副極と兼用したが、別に専用の陰分極抵抗計測装置
を設けることもできる。
In this embodiment, the sub-electrode 1 of the cathodic polarization resistance meter is also used as the sub-electrode of the cathodic protection electrometer, but a dedicated cathodic polarization resistance measuring device may be provided separately.

また演算処理回路8は電気防食用電源装置に組み込むこ
ともできる。
Further, the arithmetic processing circuit 8 can also be incorporated into a cathodic protection power supply device.

この防食方式によれば、電解式鉄イオン発生装置2は主
として初期皮膜形成の鉄イオンの供給を受は持つから、
継続的長期的な供給を前提とすることなく、銅合金チュ
ーブの面積や水量などの諸条件から初期皮膜形成に見合
った鉄イオン発生能力を有すれば良く、従来の継続的方
式のものより装置が小型小容量で、かつ電力消費量を低
減することができる。
According to this anti-corrosion method, the electrolytic iron ion generator 2 mainly supplies iron ions for initial film formation.
Without assuming continuous long-term supply, it is sufficient to have the ability to generate iron ions commensurate with the initial film formation based on various conditions such as the area of the copper alloy tube and the amount of water. is small and has a small capacity, and can reduce power consumption.

この電解式鉄イオン発生装置2によって、初期に大量な
鉄イオンの供給がなされるから、皮膜を維持するために
常時供給される鉄イオンの濃度は微量で良く、電気防食
用電極を溶解性鉄電極とすることによって十分供給でき
る。
Since a large amount of iron ions is initially supplied by this electrolytic iron ion generator 2, the concentration of iron ions constantly supplied to maintain the film only needs to be a small amount, and the electrolytic protection electrode is made of soluble iron. Sufficient supply can be achieved by using electrodes.

単に電気防食用電極に鉄電極を用いても、通電電流は防
食電流によって制約を受けるから鉄イオン供給量は少な
く、初期の皮膜形成に必要とする量に遥かに及ばない。
Even if an iron electrode is simply used as the electrode for cathodic protection, the amount of iron ion supplied is small because the applied current is limited by the corrosion protection current, and is far below the amount required for initial film formation.

したがって、鉄電極を用いる場合は従来、間欠的に硫酸
第1鉄の投入を行なっていたが、本発明の方法によれば
硫酸第1鉄を投入することな(防食皮膜の維持が可能で
ある。
Therefore, when iron electrodes are used, ferrous sulfate has conventionally been added intermittently, but according to the method of the present invention, it is possible to maintain the anticorrosive film without adding ferrous sulfate. .

また、この方式によれば、熱交換器の銅合金系チューブ
の防食において、電気防食の防食電流値と供給鉄イオン
量について、相関的に効果的制御を行なうことができる
とともに適格かつ合理的な防食管理を行うことができる
In addition, according to this method, in the corrosion protection of copper alloy tubes of heat exchangers, it is possible to effectively control the corrosion protection current value of cathodic protection and the amount of supplied iron ions in a correlated manner, and also to perform appropriate and rational control. Corrosion prevention management can be performed.

さらに、チューブの防食皮膜の状態を常に監視して防食
皮膜を適正な状態に維持するので、鉄イオンの過不足か
ら生じる伝熱効率の低下などの整置を防止することがで
きる。
Furthermore, since the state of the anticorrosive coating on the tube is constantly monitored to maintain the anticorrosive coating in an appropriate state, it is possible to prevent misalignment such as a decrease in heat transfer efficiency caused by excess or deficiency of iron ions.

【図面の簡単な説明】[Brief explanation of drawings]

図面は本発明の一実施例を示す平面図である。 1・・・・・・冷却水取水路、2・・・・・・電解式鉄
イオン発生装置、3・・・・・・復水器、4・・・・・
・電気防食用鉄電極、5・・・・・・電源装置、6・・
・・・・電気防食用電源装置、γ・・・・・・陰分極抵
抗計副極、8・・・・・・演算処理回路。
The drawing is a plan view showing an embodiment of the present invention. 1... Cooling water intake channel, 2... Electrolytic iron ion generator, 3... Condenser, 4...
・Iron electrode for cathodic protection, 5...Power supply device, 6...
...Electric protection power supply device, γ...Cathode polarization resistance meter sub-electrode, 8...Arithmetic processing circuit.

Claims (1)

【特許請求の範囲】[Claims] 1 熱交換器の銅合金系チューブの防食皮膜の形成およ
び維持において、冷却水取水路に鉄イオンを供給する電
解式鉄イオン発生装置と、熱交換器の水入口側水室内に
電気防食用電極として溶解性鉄電極を設け、前記電解式
鉄イオン発生装置により安定防食皮膜を形成するととも
に前記溶解性鉄電極により防食皮膜を維持するに際し、
銅合金系チューブの防食皮膜の状態を陰分極抵抗方式に
より計測し、この分極抵抗値をもとに電気防食の防食電
流と電解式鉄イオン発生装置とを自動的に制御し、防食
電流と鉄イオン供給量とを適正値に設定することを特徴
とする熱交換器の防食方法。
1. In forming and maintaining an anti-corrosion coating on the copper alloy tubes of the heat exchanger, an electrolytic iron ion generator that supplies iron ions to the cooling water intake channel and an electrode for cathodic protection are installed in the water chamber on the water inlet side of the heat exchanger. A soluble iron electrode is provided as a method, and a stable anti-corrosion film is formed by the electrolytic iron ion generator, and the anti-corrosion film is maintained by the soluble iron electrode.
The state of the anti-corrosion coating on the copper alloy tube is measured using the cathode polarization resistance method, and based on this polarization resistance value, the anti-corrosion current for cathodic protection and the electrolytic iron ion generator are automatically controlled. A method for preventing corrosion of a heat exchanger, characterized by setting the amount of ion supply to an appropriate value.
JP53096353A 1978-08-08 1978-08-08 Corrosion prevention method for heat exchangers Expired JPS5844200B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53096353A JPS5844200B2 (en) 1978-08-08 1978-08-08 Corrosion prevention method for heat exchangers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53096353A JPS5844200B2 (en) 1978-08-08 1978-08-08 Corrosion prevention method for heat exchangers

Publications (2)

Publication Number Publication Date
JPS5523857A JPS5523857A (en) 1980-02-20
JPS5844200B2 true JPS5844200B2 (en) 1983-10-01

Family

ID=14162623

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53096353A Expired JPS5844200B2 (en) 1978-08-08 1978-08-08 Corrosion prevention method for heat exchangers

Country Status (1)

Country Link
JP (1) JPS5844200B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5967376A (en) * 1982-10-06 1984-04-17 Toshiba Corp Preventing method for electrolytic corrosion of iron
US5042575A (en) * 1990-08-27 1991-08-27 General Motors Corporation Evaporator core having biocidal fixture

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5141577B2 (en) * 1973-08-03 1976-11-10
JPS5740221B2 (en) * 1973-08-13 1982-08-26

Also Published As

Publication number Publication date
JPS5523857A (en) 1980-02-20

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