JPH06158364A - Corrosion inhibiting method for metal in water system - Google Patents

Corrosion inhibiting method for metal in water system

Info

Publication number
JPH06158364A
JPH06158364A JP31843892A JP31843892A JPH06158364A JP H06158364 A JPH06158364 A JP H06158364A JP 31843892 A JP31843892 A JP 31843892A JP 31843892 A JP31843892 A JP 31843892A JP H06158364 A JPH06158364 A JP H06158364A
Authority
JP
Japan
Prior art keywords
water
corrosion
water system
metal
anion
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.)
Granted
Application number
JP31843892A
Other languages
Japanese (ja)
Other versions
JP3358216B2 (en
Inventor
Shoei Hirano
昭英 平野
Nobuhiro Oda
信博 織田
Takashi Watanabe
渡辺  孝
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP31843892A priority Critical patent/JP3358216B2/en
Publication of JPH06158364A publication Critical patent/JPH06158364A/en
Application granted granted Critical
Publication of JP3358216B2 publication Critical patent/JP3358216B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
    • C23F11/10Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
    • C23F11/173Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
    • C23F11/18Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using inorganic inhibitors

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Abstract

PURPOSE:To effectively prevent the corrosion of a metal in a water system without inducing the problem of environmental contamination or the like. CONSTITUTION:A corrosive ion containing water of the water system is brought into contact with an anion exchanger carrying an anticorrosive anion and a low molecular weight polymer is added into the water system. By allowing the corrosive ion in water such as Cl<->, SO4<2-> to be brought into contact with the anion exchanger carrying the aniticorrosive anion such as HCO3<->, OH<-> to ion exchange, the corrosive ion conc. in water is decreased and the corrosiveness of the water system is suppressed. A anticorrosive film is formed HCO3<-> or the like eluted by ion exchanging and Ca<2+> or the like originated from the water system on the surface of the metal by the film forming accelerating action of the low molecular weight polymer and the corrosion of the metal is more certainly inhibited.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は水系の金属の腐食抑制方
法に係り、特に淡水系における軟鋼、ステンレス鋼、
銅、銅合金などの金属の腐食を効果的に抑制する方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of inhibiting corrosion of a water-based metal, and more particularly to mild steel, stainless steel,
The present invention relates to a method for effectively suppressing corrosion of metals such as copper and copper alloys.

【0002】[0002]

【従来の技術】開放、密閉循環冷却水系、蓄熱水系、密
閉冷温水系などの淡水系で使用される各種機器や配管等
の基材として、軟鋼、ステンレス鋼、銅、銅合金等が使
用されている。淡水中に浸漬使用されているこれらの基
材は、補給水から持ち込まれる塩素イオン(Cl- )、
硫酸イオン(SO4 2- )等により腐食され、孔食を発生
させる。そこで、このような淡水系と接する金属材の腐
食を抑制するために腐食抑制剤が用いられている。
2. Description of the Prior Art Mild steel, stainless steel, copper, copper alloys, etc. are used as base materials for various equipment and pipes used in open water, closed circulation cooling water system, heat storage water system, closed cold / hot water system and other fresh water systems. There is. These substrates are immersed used in freshwater, chloride ions carried over from makeup water (Cl -),
Corrosion due to sulfate ions (SO 4 2- ) etc. causes pitting corrosion. Therefore, a corrosion inhibitor is used in order to suppress the corrosion of the metal material in contact with such a fresh water system.

【0003】従来、軟鋼、ステンレス鋼、銅又は銅合金
などの金属(合金を含む)の淡水系での腐食抑制剤とし
ては、クロム酸塩、モリブデン酸塩、亜硝酸塩、りん酸
塩、ホスホン酸塩、亜鉛塩、ベンゾトリアゾール、トリ
ルトリアゾール、メルカプトベンゾチアゾールなどが使
用されてきた。
Conventionally, as corrosion inhibitors for metals (including alloys) such as mild steel, stainless steel, copper or copper alloys in a fresh water system, chromates, molybdates, nitrites, phosphates and phosphonic acids are used. Salts, zinc salts, benzotriazole, tolyltriazole, mercaptobenzothiazole and the like have been used.

【0004】また、防食剤としてクロムイオンや亜鉛イ
オンを吸着させたOH型アニオン交換樹脂で水系を処理
し、水中に防食剤を溶出させて防食する方法も提案され
ている(特公昭48−39704号公報)。
Further, there has been proposed a method of treating an aqueous system with an OH type anion exchange resin having chromium ions or zinc ions adsorbed as an anticorrosion agent and eluting the anticorrosion agent into water to prevent corrosion (Japanese Patent Publication No. 48-39704). Issue).

【0005】さらに、循環冷却水をH型強酸性陽イオン
交換樹脂とOH型弱塩基性陰イオン交換樹脂とから成る
脱塩塔に通して冷却水中の塩類の濃縮を防止する方法が
提案されている(特開昭48−13936号公報)。
Furthermore, a method has been proposed in which the circulating cooling water is passed through a desalting tower consisting of an H-type strong acid cation exchange resin and an OH-type weakly basic anion exchange resin to prevent the concentration of salts in the cooling water. (Japanese Patent Laid-Open No. 48-13936).

【0006】[0006]

【発明が解決しようとする課題】上記従来の腐食抑制剤
を含む淡水を系外へ放出した場合、環境汚染の要因とな
る恐れがある。また、特公昭48−39704号公報記
載の方法でも、溶出したクロムや亜鉛イオンによる環境
への影響が懸念される。
When the fresh water containing the above-mentioned conventional corrosion inhibitor is released to the outside of the system, it may cause environmental pollution. Also, in the method described in JP-B-48-39704, there is concern that the eluted chromium and zinc ions may affect the environment.

【0007】このため、環境への影響の少ない腐食抑制
方法の開発が望まれている。
Therefore, there is a demand for the development of a corrosion inhibiting method which has little influence on the environment.

【0008】また、特開昭48−13936号公報記載
の方法は水中のアニオンと共にカルシウムイオン等の防
食に関与する成分まで除去しようとするものである。
Further, the method described in JP-A-48-13936 is intended to remove not only anions in water but also components such as calcium ions which are involved in anticorrosion.

【0009】本発明は上記従来の実情に鑑みてなされた
ものであって、水系の金属の腐食を環境汚染等の問題を
引き起こすことなく、有効に防止することができる水系
の金属の腐食抑制方法を提供することを目的とする。
The present invention has been made in view of the above conventional circumstances, and is a method for effectively inhibiting corrosion of a water-based metal without causing problems such as environmental pollution and the like. The purpose is to provide.

【0010】[0010]

【課題を解決するための手段】本発明の水系の金属の腐
食抑制方法は、水系の金属の腐食抑制方法であって、該
水系の腐食性イオン含有水と、防食性アニオンを担持し
たアニオン交換体とを接触させると共に、該水系に低分
子量ポリマーを添加することを特徴とする。
A method of inhibiting corrosion of a water-based metal according to the present invention is a method of inhibiting corrosion of a water-based metal, which comprises anion exchange carrying corrosive ion-containing water of the water-based anticorrosion anion. It is characterized in that a low molecular weight polymer is added to the water system while contacting with the body.

【0011】なお、本発明において、防食性アニオンと
は、それ自体防食性を示さなくてもイオン交換により水
中に溶出して、水中の溶存カチオンとの反応で防食性皮
膜を形成し得るアニオンを指す。
In the present invention, the anticorrosive anion is an anion which can be dissolved in water by ion exchange and can form an anticorrosive film by reacting with a dissolved cation even if it does not exhibit anticorrosive property. Point to.

【0012】以下に本発明を詳細に説明する。The present invention will be described in detail below.

【0013】本発明の方法においては、被処理対象水系
であるCl- ,SO4 2- 等の腐食性イオンを含む水を、
OH- ,HCO3 -などの防食性アニオンを担持したアニ
オン交換樹脂やゼオライト等のアニオン交換体と接触さ
せてイオン交換すると共に、低分子量ポリマーを添加す
る。
[0013] In the method of the present invention, Cl as an object to be processed aqueous -, water containing corrosive ions SO 4 2-like,
A low molecular weight polymer is added together with the anion exchange resin supporting anticorrosive anions such as OH and HCO 3 and anion exchanger such as zeolite for ion exchange.

【0014】これにより、水中のCl- ,SO4 2- 等の
腐食性イオンはOH- ,HCO3 -等の防食性アニオンに
イオン交換されて、その含有量が低減し、腐食性が低減
される。
As a result, corrosive ions such as Cl and SO 4 2− in water are ion-exchanged with anticorrosive anions such as OH and HCO 3 , the content thereof is reduced, and the corrosiveness is reduced. It

【0015】また、低分子量ポリマーの添加により、上
記イオン交換で水中に溶出したOH- ,HCO3 -等の防
食性アニオンや水系由来のCa2+,SiO2 等の防食性
成分の均一な防食皮膜が効果的に金属表面に形成され、
腐食がより一層確実に抑制される。
Further, by adding a low-molecular weight polymer, a uniform anticorrosion of anticorrosion anions such as OH and HCO 3 dissolved in water by the above-mentioned ion exchange and anticorrosion components such as Ca 2+ and SiO 2 derived from an aqueous system. A film is effectively formed on the metal surface,
Corrosion is suppressed even more reliably.

【0016】水系の腐食イオン含有水を防食性アニオン
を担持したアニオン交換体と接触させる方法としては特
に制限はないが、例えば、防食性アニオンを担持したア
ニオン交換樹脂、具体的にはHCO3 形アニオン交換樹
脂を充填した充填塔に補給水または循環水を通水接触さ
せれば良い。この場合の通水条件等は、被処理対象水系
の水質等に応じて適宜決定される。
There is no particular limitation on the method of contacting the water-based water containing corrosive ions with the anion exchanger carrying the anticorrosion anion. For example, anion exchange resin carrying the anticorrosion anion, specifically HCO 3 type Make-up water or circulating water may be brought into water contact with a packed tower filled with an anion exchange resin. The water flow conditions and the like in this case are appropriately determined according to the water quality and the like of the water system to be treated.

【0017】一方、低分子量ポリマーとしては、分子量
500〜100,000、特に1000〜20,000
程度の水溶性のポリマー、具体的には、マレイン酸−イ
ソブチレン共重合体、ポリアクリル酸、ポリアクリルア
ミドの部分加水分解物、アクリル酸−アリロキシ−2−
ヒドロキシプロパンスルホン酸共重合体、アクリル酸−
ヒドロキシエチルメタクリル酸共重合体、アクリルアミ
ドとアリルスルホン酸共重合体、アクリル酸−マレイン
酸共重合体、アクリル酸−スチレン共重合体、アクリル
酸−スチレンスルホン酸共重合体、ポリマレイン酸、ポ
リスチレンスルホン酸、アクリル酸−イタコン酸共重合
体、ポリイタコン酸、アクリル酸−アクリロニトリル共
重合体、アクリル酸−ビニルスルホン酸共重合体、メチ
ルビニルエーテル−マレイン酸共重合体など公知の低分
子量ポリマーが挙げられる。
On the other hand, the low molecular weight polymer has a molecular weight of 500 to 100,000, particularly 1000 to 20,000.
Water-soluble polymer to a certain extent, specifically, maleic acid-isobutylene copolymer, polyacrylic acid, partial hydrolyzate of polyacrylamide, acrylic acid-allyloxy-2-
Hydroxypropanesulfonic acid copolymer, acrylic acid-
Hydroxyethyl methacrylic acid copolymer, acrylamide and allyl sulfonic acid copolymer, acrylic acid-maleic acid copolymer, acrylic acid-styrene copolymer, acrylic acid-styrene sulfonic acid copolymer, polymaleic acid, polystyrene sulfonic acid Examples thereof include known low molecular weight polymers such as acrylic acid-itaconic acid copolymer, polyitaconic acid, acrylic acid-acrylonitrile copolymer, acrylic acid-vinyl sulfonic acid copolymer, and methyl vinyl ether-maleic acid copolymer.

【0018】このような低分子量ポリマーの添加量は被
処理水系の水質によっても異なるが、通常の場合、被処
理水に対して0.1〜500mg/l添加する。
The addition amount of such a low molecular weight polymer varies depending on the water quality of the water to be treated, but in the usual case, it is added in an amount of 0.1 to 500 mg / l to the water to be treated.

【0019】なお、低分子量ポリマーの添加時期には特
に制限はないが、通常の場合、前記アニオン交換体によ
る処理のあととするのが好ましい。
The addition timing of the low molecular weight polymer is not particularly limited, but in the usual case, it is preferably after the treatment with the anion exchanger.

【0020】このような本発明の方法は、腐食性イオン
としてCl- ,SO4 2- を含有する水系、例えば淡水系
の金属の腐食抑制に極めて有効である。
The method of the present invention as described above is extremely effective in inhibiting corrosion of water-based metals, such as fresh water-based metals, containing Cl and SO 4 2− as corrosive ions.

【0021】このように本発明は上記の構成により環境
問題を引き起こすことなく水素の防食処理を達成し得る
ものであるが、必要に応じて、無機リン酸塩(正リン酸
塩や重合リン酸塩)や有機リン酸エステル、ホスホン酸
類、亜鉛、ニッケル塩、タングステン酸塩、モリブデン
酸塩、亜硝酸塩、ホウ酸塩、ケイ酸塩、オキシカルボン
酸塩、ベンゾトリアゾール、メルカプトベンゾチアゾー
ル等の防食剤やリグニン誘導体、タンニン酸類、テンプ
ン等の多糖類等のスケール防止剤等を併用してもよい。
As described above, according to the present invention, the anticorrosion treatment of hydrogen can be achieved without causing environmental problems by the above-mentioned constitution. However, if necessary, inorganic phosphate (orthophosphate or polymerized phosphate) can be used. Salts), organic phosphates, phosphonic acids, zinc, nickel salts, tungstates, molybdates, nitrites, borates, silicates, oxycarboxylates, benzotriazole, mercaptobenzothiazole, and other anticorrosive agents Alternatively, scale inhibitors such as lignin derivatives, tannic acids, and polysaccharides such as tempun may be used in combination.

【0022】[0022]

【作用】Cl- ,SO4 2- 等の水中の腐食性イオンをH
CO3 -,OH- 等の防食性アニオンを担持したアニオン
交換体と接触させてイオン交換することにより、水中の
腐食性イオン濃度が低減し、水系の腐食性が緩和され
る。
[Action] Cl -, water corrosive ions SO 4 2-like H
By contacting with an anion exchanger carrying an anticorrosive anion such as CO 3 or OH to carry out ion exchange, the concentration of corrosive ions in water is reduced and the corrosiveness of the water system is mitigated.

【0023】また、低分子量ポリマーの皮膜形成促進作
用により、イオン交換で溶出したHCO3 -等と水系由来
のCa2+等とが金属表面に防食皮膜を形成し、金属の腐
食はより一層確実に抑制される。
Further, due to the film formation-promoting action of the low molecular weight polymer, HCO 3 etc. eluted by ion exchange and Ca 2+ etc. derived from the water system form an anticorrosion film on the metal surface, so that metal corrosion is more reliable. Suppressed to.

【0024】即ち、腐食性アニオンであるCl- の低減
は軟鋼やステンレス鋼、銅、黄銅等の孔食抑制に有効で
ある上に、ステンレス鋼や黄銅にしばしば生じる応力腐
食割れの有効な防止対策となる。
[0024] That is, a corrosive anions Cl - Reducing of mild steel and stainless steel, copper, on an effective pitting inhibition such as brass, effective prevention of the frequently occurring stress corrosion cracking in stainless steel and brass Becomes

【0025】また、SO4 2- の低減により、銅や黄銅に
対し、孔食発生の要因となる塩基性硫酸銅の生成が防止
され、腐食が抑制される。
Further, the reduction of SO 4 2− prevents the formation of basic copper sulfate, which causes pitting corrosion, with respect to copper and brass, and suppresses corrosion.

【0026】一方、防食性イオンであるCa2+やHCO
3 -は、低分子量ポリマーの存在下、金属表面にCaCO
3 の均一な沈殿皮膜を形成し、腐食促進の要因である溶
存酸素の拡散を防止することにより、腐食を抑制する。
On the other hand, Ca 2+ and HCO which are anticorrosive ions
3 - is CaCO on the metal surface in the presence of low molecular weight polymer.
Corrosion is suppressed by forming a uniform precipitate film of 3 and preventing the diffusion of dissolved oxygen which is a factor promoting corrosion.

【0027】水中のSiO2 は軟鋼の錆を固着性に変質
させ腐食を抑制する作用を奏する。
SiO 2 in water has the function of changing the rust of mild steel to a sticky property and suppressing corrosion.

【0028】[0028]

【実施例】以下に実施例を挙げて本発明をより具体的に
説明する。
EXAMPLES The present invention will be described in more detail with reference to the following examples.

【0029】実施例1試験水の調製 強塩基性アニオン交換樹脂「レバチットM500」1リ
ットルを内径38mm,長さ1000mmのアクリルカ
ラムに充填し、5%NaHCO3 水溶液で再生してHC
3 形とした後水洗した。このHCO3 形アニオン交換
樹脂塔に、表1に示す水質の人工淡水a液,b液,c液
を、それぞれ、50リットル/hrの流量で通水してア
ニオン交換処理したところ、それぞれ表1に示す水質の
a´液,b´液,c´液が得られた。
Example 1 Preparation of test water 1 liter of a strongly basic anion exchange resin "Levacit M500" was packed in an acrylic column having an inner diameter of 38 mm and a length of 1000 mm, and regenerated with a 5% NaHCO 3 aqueous solution to generate HC.
It was made O 3 type and washed with water. The HCO 3 type anion exchange resin tower was subjected to anion exchange treatment by passing water of artificial water A, B, and C having the water quality shown in Table 1 at a flow rate of 50 liters / hr. Liquids a ', b', and c'shown in water quality were obtained.

【0030】[0030]

【表1】 [Table 1]

【0031】別に、水溶性低分子量ポリマーとして分子
量約15,000の無水マレイン酸−イソブチレン共重
合体「イソバンKPS−3」を12mg/l添加した表
2に示す水質の人工淡水A液,B液,C液をそれぞれ上
記と同様の方法でアニオン交換処理したところ、それぞ
れ表2に示す水質のA´液,B´液,C´液が得られ
た。
Separately, 12 mg / l of maleic anhydride-isobutylene copolymer "Isoban KPS-3" having a molecular weight of about 15,000 was added as a water-soluble low-molecular weight polymer. , C liquid were subjected to anion exchange treatment in the same manner as described above, and the water quality A'solution, B'solution and C'solution shown in Table 2 were obtained.

【0032】[0032]

【表2】 [Table 2]

【0033】腐食試験 試験水を入れた1リットル容のガラスビーカーに、先端
に軟鋼製テストピースを取り付けた塩化ビニル製回転軸
を挿入して、試験水中で回転させる回転腐食試験装置を
用いて腐食試験を行なった。
Corrosion test Insert a vinyl chloride rotary shaft with a mild steel test piece at the tip into a glass beaker of 1 liter containing test water, and use a rotary corrosion tester to rotate in test water. The test was conducted.

【0034】試験温度は50℃、試験水量は1リット
ル、試験期間は4日間、回転軸の回転速度は180r.
p.m.とした。テストピースはSPCC材よりなる表
面積31cm2 のものを、400番のエメリー研磨紙で
研磨した後、脱脂して試験に供した。試験結果(腐食減
量、腐食速度)を表3に示す。
The test temperature was 50 ° C., the test water amount was 1 liter, the test period was 4 days, and the rotation speed of the rotary shaft was 180 rpm.
p. m. And A test piece having a surface area of 31 cm 2 made of SPCC material was polished with No. 400 emery polishing paper, degreased, and used for the test. Table 3 shows the test results (corrosion weight loss, corrosion rate).

【0035】[0035]

【表3】 [Table 3]

【0036】上記結果より、次のことが明らかである。
即ち、特に、a液とa´液との腐食試験の結果の比較に
より、淡水をアニオン交換処理することにより、腐食性
が著しく緩和される。
From the above results, the following is clear.
That is, in particular, by comparing the results of the corrosion tests of the liquid a and the liquid a ′, the corrosiveness is remarkably reduced by the anion exchange treatment of fresh water.

【0037】なお、硬度が比較的高いb液,c液をアニ
オン交換したb´液,c´液では水中でCaCO3 が析
出するため、アニオン交換処理による腐食抑制効果が現
れない。なお、このCaCO3 の析出は、表1に示すc
´液,b´液のカルシウム硬度がそれぞれ144,26
0mg/lあるべきところ、28,12mg/lとなっ
ていることから明らかである。即ち、これらb´液,c
´液では、アニオン交換処理によりMアルカリ度が高く
なるため、CaCO3 が析出し易い条件となっている。
In addition, since CaCO 3 is precipitated in water in the b'solution and the c'solution obtained by anion-exchange of the b-solution and the c-solution having a relatively high hardness, the anion-exchange treatment does not exhibit the corrosion inhibiting effect. The precipitation of CaCO 3 is c as shown in Table 1.
Calcium hardness of liquid'b 'is 144,26
It is obvious from the fact that it should be 0 mg / l, but 28,12 mg / l. That is, these b'solution, c
Since the M alkalinity is increased by the anion exchange treatment in the liquid ', the condition is that CaCO 3 is likely to precipitate.

【0038】しかし、このように硬度の高い液であって
も水溶性低分子量ポリマーを添加し、水中でのCaCO
3 の析出を防止するように制御した場合には、B液,C
液とB´液,C´液の腐食試験結果の比較から明らかな
ように、CaCO3 は効果的に軟鋼製テストピースの表
面に均一皮膜として析出するようになり、防食効果は著
しく高められる。
However, even in such a liquid having high hardness, a water-soluble low-molecular weight polymer is added, and CaCO in water is added.
When controlling so as to prevent precipitation of 3 , B liquid, C
As is clear from the comparison of the corrosion test results of the liquid, the B'solution, and the C'solution, CaCO 3 is effectively deposited as a uniform film on the surface of the mild steel test piece, and the anticorrosion effect is significantly enhanced.

【0039】以上より、水中の腐食性イオンを防食性ア
ニオンでイオン交換すると共に低分子量ポリマーを添加
することにより、水中の硬度に関係なく、金属の腐食を
確実に抑制することができることが明らかである。
From the above, it is clear that by exchanging corrosive ions in water with anticorrosive anions and adding a low molecular weight polymer, it is possible to reliably suppress metal corrosion regardless of hardness in water. is there.

【0040】[0040]

【発明の効果】以上詳述した通り、本発明の水系の金属
の腐食抑制方法によれば、水系の腐食性イオンをアニオ
ン交換により低減すると共に、アニオン交換により溶出
した防食性イオン、水系由来の防食性イオンを有効利用
して、低分子量ポリマーの皮膜形成促進作用で均一な防
食皮膜を金属表面に効率的に析出形成させることによ
り、金属の腐食を、環境に悪影響を及ぼすことなく、確
実に防止することが可能とされる。
As described in detail above, according to the method of inhibiting corrosion of a metal in the water system of the present invention, the corrosive ions in the water system are reduced by anion exchange, and at the same time, the anticorrosive ions eluted by the anion exchange and water-derived By effectively utilizing the anticorrosive ions, a uniform anticorrosive film is efficiently deposited and formed on the metal surface by the film formation promoting action of the low molecular weight polymer, so that metal corrosion can be ensured without adversely affecting the environment. It is possible to prevent it.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 水系の金属の腐食抑制方法であって、該
水系の腐食性イオン含有水と、防食性アニオンを担持し
たアニオン交換体とを接触させると共に、該水系に低分
子量ポリマーを添加することを特徴とする水系の金属の
腐食抑制方法。
1. A method for inhibiting corrosion of a water-based metal, which comprises contacting the water-based water containing corrosive ions with an anion exchanger carrying an anticorrosive anion, and adding a low molecular weight polymer to the water-based system. A method for inhibiting corrosion of a water-based metal, which is characterized by the above.
JP31843892A 1992-11-27 1992-11-27 Water-based metal corrosion suppression method Expired - Fee Related JP3358216B2 (en)

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JPH06158364A true JPH06158364A (en) 1994-06-07
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Country Link
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0857514A2 (en) * 1997-01-09 1998-08-12 Kurita Water Industries Ltd. Method of preventing corrosion in a water system
EP0866148A1 (en) * 1995-12-27 1998-09-23 Kurita Water Industries Ltd. Method for inhibiting corrosion in water systems
JP2006234421A (en) * 2005-02-22 2006-09-07 Kobe Steel Ltd Accelerated test method of stress corrosion cracking
JP2009028724A (en) * 2001-04-05 2009-02-12 Toray Ind Inc Method for water treatment and apparatus for water treatment
WO2009137636A1 (en) 2008-05-07 2009-11-12 Nalco Company Method of minimizing corrosion, scale, and water consumption in cooling tower systems
JP2010059091A (en) * 2008-09-03 2010-03-18 Tosoh Corp t-BUTYL ALCOHOL SOLUTION AND METHOD FOR PRODUCING THE SAME
JP2016035081A (en) * 2014-08-01 2016-03-17 東京電力株式会社 Corrosion inhibition method for ferrous material in fresh water environment

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0866148B1 (en) * 1995-12-27 2001-09-19 Kurita Water Industries Ltd. Method for inhibiting corrosion in water systems
EP0866148A1 (en) * 1995-12-27 1998-09-23 Kurita Water Industries Ltd. Method for inhibiting corrosion in water systems
US5820763A (en) * 1995-12-27 1998-10-13 Kurita Water Industries, Ltd. Method for inhibiting corrosion in water systems
EP1405671A2 (en) * 1997-01-09 2004-04-07 Kurita Water Industries Ltd. Method of preventing corrosion in a water system
US5985152A (en) * 1997-01-09 1999-11-16 Kurita Water Industries Ltd. Method of preventing corrosion in a water system
EP0857514A3 (en) * 1997-01-09 1999-03-17 Kurita Water Industries Ltd. Method of preventing corrosion in a water system
EP0857514A2 (en) * 1997-01-09 1998-08-12 Kurita Water Industries Ltd. Method of preventing corrosion in a water system
EP1405671A3 (en) * 1997-01-09 2004-06-30 Kurita Water Industries Ltd. Method of preventing corrosion in a water system
JP2009028724A (en) * 2001-04-05 2009-02-12 Toray Ind Inc Method for water treatment and apparatus for water treatment
JP2006234421A (en) * 2005-02-22 2006-09-07 Kobe Steel Ltd Accelerated test method of stress corrosion cracking
JP4519680B2 (en) * 2005-02-22 2010-08-04 株式会社神戸製鋼所 Accelerated testing method for stress corrosion cracking
WO2009137636A1 (en) 2008-05-07 2009-11-12 Nalco Company Method of minimizing corrosion, scale, and water consumption in cooling tower systems
JP2010059091A (en) * 2008-09-03 2010-03-18 Tosoh Corp t-BUTYL ALCOHOL SOLUTION AND METHOD FOR PRODUCING THE SAME
JP2016035081A (en) * 2014-08-01 2016-03-17 東京電力株式会社 Corrosion inhibition method for ferrous material in fresh water environment

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