JP4244983B2 - Metal corrosion control method - Google Patents

Metal corrosion control method Download PDF

Info

Publication number
JP4244983B2
JP4244983B2 JP2005312980A JP2005312980A JP4244983B2 JP 4244983 B2 JP4244983 B2 JP 4244983B2 JP 2005312980 A JP2005312980 A JP 2005312980A JP 2005312980 A JP2005312980 A JP 2005312980A JP 4244983 B2 JP4244983 B2 JP 4244983B2
Authority
JP
Japan
Prior art keywords
polymer
water
corrosion
metal
maleic acid
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
Application number
JP2005312980A
Other languages
Japanese (ja)
Other versions
JP2007119835A (en
Inventor
一 井芹
藤田  和久
裕 米田
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 JP2005312980A priority Critical patent/JP4244983B2/en
Publication of JP2007119835A publication Critical patent/JP2007119835A/en
Application granted granted Critical
Publication of JP4244983B2 publication Critical patent/JP4244983B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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

Landscapes

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

Description

本発明は、金属の腐食抑制方法に係り、特に毒性や閉鎖性水域における富栄養化等の環境汚染問題を発生させることなく、水と接触する金属、特に鋼材の腐食を効果的に抑制する方法に関するものである。   The present invention relates to a method for inhibiting corrosion of metal, and in particular, a method for effectively inhibiting corrosion of a metal in contact with water, particularly a steel material, without causing environmental pollution problems such as toxicity and eutrophication in closed water areas. It is about.

冷却水系に設けられた金属部材、例えば、炭素鋼、銅、又は銅合金製の熱交換器や反応釜、配管は、冷却水と接触することにより腐食を受けることから、一般に、薬剤添加による防食処理が施されている。   Metal members provided in the cooling water system, such as heat exchangers, reaction kettles and piping made of carbon steel, copper, or copper alloys, are generally corroded by contact with cooling water. Processing has been applied.

例えば、炭素鋼製の熱交換器、反応釜や配管の腐食を抑制するために、従来、オルトリン酸塩、ヘキサメタリン酸塩、ヒドロキシエチリデンジホスホン酸塩、ホスホノブタントリカルボン酸塩などのリン化合物が冷却水に添加されている。また、亜鉛塩や重クロム酸塩のような重金属塩を単独で或いは併用して添加する場合もある。しかし、これらのリン化合物や重金属塩の大量使用、特に重金属塩の大量使用は、水質を汚染し環境に重篤な影響を招く恐れがあるため、その取り扱いや排水処理に多大な注意と費用が必要になる。   For example, phosphorus compounds such as orthophosphate, hexametaphosphate, hydroxyethylidene diphosphonate, and phosphonobutanetricarboxylate have been conventionally used to suppress corrosion of carbon steel heat exchangers, reaction kettles and piping. It is added to the cooling water. Further, a heavy metal salt such as zinc salt or dichromate may be added alone or in combination. However, large amounts of these phosphorus compounds and heavy metal salts, especially heavy metal salts, can contaminate the water quality and have a serious impact on the environment. I need it.

このような環境問題を引き起こすことなく金属の腐食を効果的に抑制する方法として、マレイン酸とイソブチレンの共重合体を添加し、ランジェリア指数を1.5以上かつシリカ濃度とカルシウム硬度の積を2000以上として管理する腐食抑制方法(特許1806295号)が開示されている。   As a method for effectively suppressing the corrosion of metals without causing such environmental problems, a copolymer of maleic acid and isobutylene is added, the Langerian index is 1.5 or more, and the product of silica concentration and calcium hardness is increased. A corrosion suppression method (Japanese Patent No. 1806295) that is managed as 2000 or more is disclosed.

また、補正リツナー指数が3.0〜6.0になるように調整した循環水中に190nmにおける吸光係数が0.09〜0.2mg−1・dm・cm−1である水溶性マレイン酸重合体を添加する金属の腐食抑制方法(特開2004−91835)が開示されている。 In addition, water-soluble maleic acid heavy acid having an extinction coefficient at 190 nm of 0.09 to 0.2 mg −1 · dm 3 · cm −1 in circulating water adjusted so that the corrected Ritzner index is 3.0 to 6.0. A method for inhibiting corrosion of a metal to which a coalescence is added (Japanese Patent Application Laid-Open No. 2004-91835) is disclosed.

これらの技術を用い、適正な管理を行うことにより、冷却水系の腐食を抑制することができるが、より一層効果的な腐食抑制技術の開発が望まれている。
特許1806295号 特開2004−91835
By using these techniques and performing appropriate management, corrosion of the cooling water system can be suppressed, but development of a more effective corrosion suppression technique is desired.
Patent 1806295 JP 2004-91835 A

本発明は、環境汚染問題を惹き起こすことなく、かつ公知の腐食抑制方法よりも優れた効果を発揮する金属の腐食抑制方法を提供することを目的とする。   An object of the present invention is to provide a method for inhibiting corrosion of a metal that does not cause environmental pollution problems and exhibits an effect superior to that of known corrosion inhibition methods.

本発明者らは、上記課題を解決すべく、水中に存在するカルシウム、シリカ、Mアルカリ度等の防食成分を有効に利用できる方法の検討を行った結果、特定のランジェリア指数、特定の[SiO]×[CaH]値となるように水質を調整した水系に、特定の2種類のポリマーを添加することにより、公知技術よりも優れた防食効果が得られることを見出し、本発明を完成させた。
即ち、本発明は以下を要旨とする。
[1] 水系の金属の腐食を抑制する方法において、ランジェリア指数が1.5以上で、かつ[SiO]×[CaH]≧2000(ただし、[SiO]は水中のSiO濃度(mg/L)、[CaH]は水中のCaCOとしてのカルシウム硬度(mg/L))となるように調整された該水系の水に、マレイン酸及び/又はその水溶性塩から選ばれる1種以上の重合体(以下、「重合体A」と称す。)と、マレイン酸、無水マレイン酸及びこれらの水溶性塩から選ばれる1種以上と非イオン性モノエチレン系不飽和単量体の1種以上との共重合体(以下、「重合体B」と称す。)とを添加する金属の腐食抑制方法であって、重合体Aと重合体Bとを固形分濃度比で重合体A:重合体B=1:4〜4:1の範囲となるように該水系に添加することを特徴とする金属の腐食抑制方法。
] [1]において、重合体Bの非イオン性モノエチレン系不飽和単量体がイソブチレンであることを特徴とする金属の腐食抑制方法。
[3] [1]又は[2]において、重合体Aと重合体Bとを固形分濃度比で重合体A:重合体B=1:2〜2:1の範囲となるように該水系に添加することを特徴とする金属の腐食抑制方法。
[4]1]ないし[3]のいずれかにおいて、重合体Aの分子量が800〜1500であることを特徴とする金属の腐食抑制方法。
[5]1]ないし[4]のいずれかにおいて、重合体Bを構成するマレイン酸成分と非イオン性エチレン成分との合計100モル%に対してマレイン酸成分が25〜75モル%の重合体Bを用いることを特徴とする金属の腐食抑制方法。
In order to solve the above problems, the present inventors have studied a method that can effectively use anticorrosive ingredients such as calcium, silica, and M alkalinity existing in water, and as a result, a specific Langerian index, a specific [ It was found that the anticorrosion effect superior to the known technique can be obtained by adding two specific types of polymers to an aqueous system whose water quality is adjusted so as to have a SiO 2 ] × [CaH] value, and the present invention is completed. I let you.
That is, the gist of the present invention is as follows.
[1] In the method for suppressing corrosion of an aqueous metal, the Langeria index is 1.5 or more, and [SiO 2 ] × [CaH] ≧ 2000 (where [SiO 2 ] is the concentration of SiO 2 in water (mg / L), [CaH] is one or more selected from maleic acid and / or water-soluble salts thereof in the aqueous water adjusted to have calcium hardness (mg / L) as CaCO 3 in water A polymer (hereinafter referred to as “polymer A”), one or more selected from maleic acid, maleic anhydride, and water-soluble salts thereof, and one nonionic monoethylenically unsaturated monomer A method for inhibiting corrosion of a metal by adding a copolymer (hereinafter referred to as “polymer B”) to the polymer A and the polymer B in a solid content concentration ratio. Addition to the aqueous system so that coalescence B = 1: 4-4: 1 Metal method corrosion inhibition, characterized in that that.
[2] Oite to [1], metal method corrosion inhibition, wherein the non-ionic monoethylenically unsaturated monomer is isobutylene polymer B.
[3] In [1] or [2], the polymer A and the polymer B are mixed in the aqueous system so that the solid content concentration ratio is in the range of polymer A: polymer B = 1: 2 to 2: 1. A method for inhibiting corrosion of a metal, comprising adding the metal.
[4] The method for inhibiting corrosion of a metal according to any one of [ 1] to [3], wherein the molecular weight of the polymer A is 800 to 1500.
[5] In any one of [ 1] to [4], the weight of maleic acid component is 25 to 75 mol% with respect to 100 mol% of the total of maleic acid component and nonionic ethylene component constituting polymer B. A method for inhibiting corrosion of a metal, characterized by using coalescence B.

本発明の金属の腐食抑制方法によれば、リン系化合物や重金属塩を使用することなく、従って、環境汚染問題を惹き起こすことなく、水系の金属の腐食を効果的に防止あるいは抑制することが可能となり、冷却水系等の安定運転に寄与することができる。   According to the method for inhibiting corrosion of a metal of the present invention, it is possible to effectively prevent or inhibit corrosion of an aqueous metal without using a phosphorus compound or a heavy metal salt, and without causing environmental pollution problems. It becomes possible and can contribute to stable operation of a cooling water system or the like.

なお、本発明において、
(1) ランジェリア指数≧1.5
(2) [SiO]×[CaH]≧2000の水系に
(3) 重合体Aと重合体Bとを添加する
という、(1)〜(3)の要件は極めて重要であり、本発明においては、これらのうちの1条件でも欠けると良好な効果は得られない。
In the present invention,
(1) Langeria index ≧ 1.5
(2) To an aqueous system of [SiO 2 ] × [CaH] ≧ 2000
(3) The requirement of (1) to (3) that the polymer A and the polymer B are added is very important. In the present invention, if one of these conditions is missing, a good effect can be obtained. I can't.

例えばランジェリア指数が1.5以上で[SiO]×[CaH]≧2000の水系であっても、重合体Aと重合体Bの一方のみの添加では、十分な防食効果は得られない。また、重合体Aと重合体Bとを添加しても、水系の水質が(1)及び/又は(2)を満たさない場合には、良好な防食効果は得られない。 For example, even in the case of an aqueous system having a Langeria index of 1.5 or more and [SiO 2 ] × [CaH] ≧ 2000, the addition of only one of the polymer A and the polymer B cannot provide a sufficient anticorrosive effect. Further, even when the polymer A and the polymer B are added, if the water quality of the aqueous system does not satisfy (1) and / or (2), a good anticorrosive effect cannot be obtained.

一般に、開放循環冷却水等の水系において、水の濃縮度を上げると、水中に含まれるカルシウムイオンや重炭酸イオンの濃度及びpHは増加し、CaCO皮膜の生成により腐食が抑制されることはよく知られている。この水系のCaCO析出傾向を示す尺度として、ランジェリアの飽和指数が提案されている。これは、カルシウム濃度、Mアルカリ度、全溶解固形物及び水温、pHから、その水のCaCO析出傾向を一つの目安として示すものである。しかして、このランジェリア指数が1.5以上であると、CaCOのスケールが付着する傾向が大きくなるため、水の防食性も大きくなる。 Generally, in an aqueous system such as open circulation cooling water, when the concentration of water is increased, the concentration and pH of calcium ions and bicarbonate ions contained in the water are increased, and corrosion is suppressed by the formation of a CaCO 3 film. well known. As a scale indicating the water-based CaCO 3 precipitation tendency, the Langerian saturation index has been proposed. This shows the CaCO 3 precipitation tendency of the water as one standard from the calcium concentration, M alkalinity, total dissolved solid, water temperature, and pH. Accordingly, when the Langeria index is 1.5 or more, the CaCO 3 scale tends to adhere, and the corrosion resistance of water also increases.

また、水系に含有されるシリカも防食上極めて重要な役割を果す。しかるに、ランジェリア指数には、水系のシリカ含有量は全溶解固形物の1種として扱われており、ランジェリア指数にはシリカ濃度が直接的に表示されていない。   Silica contained in the water system also plays an extremely important role in preventing corrosion. However, the silica content of the aqueous system is treated as one of the total dissolved solids in the Langeria index, and the silica concentration is not directly displayed in the Langeria index.

そこで、良好な防食効果が得られる水系のシリカ濃度について検討した結果、ランジェリア指数が1.5以上のもののうち、特に[SiO]×[CaH]≧2000のもののみが、本発明に係る重合体Aと重合体Bとの併用による相乗効果において共奏効果を発揮することが解明された。 Therefore, as a result of examining the silica concentration in water based on which a good anticorrosive effect can be obtained, only those having [SiO 2 ] × [CaH] ≧ 2000 in particular according to the present invention out of those having a Langeria index of 1.5 or more. It has been elucidated that the synergistic effect of the combined use of the polymer A and the polymer B exhibits a concerto effect.

本発明において、重合体Aと重合体Bとは、固形分濃度比で重合体A:重合体B=1:4〜4:1の範囲となるように添加することが好ましい(請求項2)。また、重合体Bの非イオン性モノエチレン系不飽和単量体としては、イソブチレンが好ましい(請求項3)。   In the present invention, the polymer A and the polymer B are preferably added so that the solid content concentration ratio is in the range of polymer A: polymer B = 1: 4 to 4: 1 (Claim 2). . Further, as the nonionic monoethylenically unsaturated monomer of the polymer B, isobutylene is preferable (Claim 3).

以下に本発明の金属の腐食抑制方法の実施の形態を詳細に説明する。
なお、本発明において、「分子量」とは「重量平均分子量」を指す。
Embodiments of the metal corrosion inhibiting method of the present invention will be described in detail below.
In the present invention, “molecular weight” refers to “weight average molecular weight”.

[重合体A]
重合体Aは、マレイン酸及び/又はマレイン酸の水溶性塩の重合体である。
ここで、マレイン酸の水溶性塩としては、マレイン酸ナトリウム、マレイン酸カリウム、マレイン酸アンモニウム等が挙げられる。
重合体Aの分子量としては、500〜5000程度、特に800〜1500程度であることが好ましい。
[Polymer A]
The polymer A is a polymer of maleic acid and / or a water-soluble salt of maleic acid.
Here, examples of the water-soluble salt of maleic acid include sodium maleate, potassium maleate, and ammonium maleate.
The molecular weight of the polymer A is preferably about 500 to 5000, particularly about 800 to 1500.

[重合体B]
重合体Bは、マレイン酸、無水マレイン酸及びこれらの水溶性塩から選ばれる1種以上(以下、「マレイン酸成分」と称す。)と非イオン性モノエチレン系不飽和単量体1種以上(以下「非イオン性エチレン成分」と称す。)との共重合体である。
マレイン酸成分の水溶性塩としては、ナトリウム塩、カリウム塩、アンモニウム塩等が挙げられる。
[Polymer B]
Polymer B is at least one selected from maleic acid, maleic anhydride and water-soluble salts thereof (hereinafter referred to as “maleic acid component”) and at least one nonionic monoethylenically unsaturated monomer. (Hereinafter referred to as “nonionic ethylene component”).
Examples of the water-soluble salt of the maleic acid component include sodium salt, potassium salt, ammonium salt and the like.

非イオン性エチレン成分としては、炭素数2〜8のオレフィン炭化水素が挙げられ、例えばイソブチレン、エチレン、プロピレン、ブチレン、1−ペンテン、1−ヘキセン、1−オクテン等が好ましく、特にイソブチレンが好ましい。   Examples of the nonionic ethylene component include olefin hydrocarbons having 2 to 8 carbon atoms. For example, isobutylene, ethylene, propylene, butylene, 1-pentene, 1-hexene, 1-octene and the like are preferable, and isobutylene is particularly preferable.

重合体Bを構成するマレイン酸成分と非イオン性エチレン成分との合計100モル%に対してマレイン酸成分が10モル%以上、好ましくは25〜75モル%の重合体Bを用いることが好ましい。   It is preferable to use the polymer B in which the maleic acid component is 10 mol% or more, preferably 25 to 75 mol%, based on the total 100 mol% of the maleic acid component and the nonionic ethylene component constituting the polymer B.

また、重合体Bの分子量は5000〜50000程度、特に10000〜30000程度であることが好ましい。   Moreover, it is preferable that the molecular weight of the polymer B is about 5000-50000, especially about 10,000-30000.

[水質調整]
本発明においては、処理対象水系の水を、ランジェリア指数が1.5以上で、かつ[SiO]×[CaH]≧2000(ただし、[SiO]は水中のSiO濃度(mg/L)、[CaH]は水中のCaCOとしてのカルシウム硬度(mg/L))となるように調整する。
[Water quality adjustment]
In the present invention, water in the water system to be treated has a Langeria index of 1.5 or more and [SiO 2 ] × [CaH] ≧ 2000 (where [SiO 2 ] is the concentration of SiO 2 in water (mg / L ) And [CaH] are adjusted so as to have a calcium hardness (mg / L) as CaCO 3 in water.

処理対象水のランジェリア指数と[SiO]×[CaH]がこのような特定値以上となるように、水中にCaCO及びシリカが含有されていると、この水に添加された重合体Aと重合体Bとが確実にCaCO等をまき込んで、金属表面に良好な防食皮膜を形成し、優れた防食抑制効果が得られる。ランジェリア指数が1.5未満でも、[SiO]×[CaO]<2000でも、良好な腐食抑制効果が得られない。従って、処理対象水系がこの規定値をはずれるような水質であった場合には、重合体Aと重合体Bとの添加に先立って、処理対象水の水質を調整する。 If CaCO 3 and silica are contained in the water so that the Langerian index and [SiO 2 ] × [CaH] of the water to be treated are not less than the specific value, the polymer A added to the water And polymer B surely entrap CaCO 3 or the like to form a good anticorrosive film on the metal surface, and an excellent anticorrosive effect can be obtained. Even if the Langeria index is less than 1.5, even if [SiO 2 ] × [CaO] <2000, a good corrosion inhibiting effect cannot be obtained. Therefore, when the water quality of the water to be treated is such that it does not exceed this specified value, the water quality of the water to be treated is adjusted prior to the addition of the polymer A and the polymer B.

この水質の調整方法としては特に制限はないが、例えば、開放循環冷却水系等であれば、水の濃縮度を上げる方法が挙げられる。その他、水質の調整は必要な成分を水系へ添加することによっても行うことができる。   Although there is no restriction | limiting in particular as this water quality adjustment method, For example, if it is an open circulation cooling water system etc., the method of raising the concentration of water will be mentioned. In addition, the water quality can be adjusted by adding necessary components to the aqueous system.

[固形分濃度比及び添加濃度]
重合体Aと重合体Bとは、固形分濃度比が重合体A:重合体B=1:4〜4:1、好ましくは1:2〜2:1となるように処理対象水系に添加する。この使用割合が上記範囲をはずれると良好な腐食抑制効果が得られない。
[Solid content concentration ratio and additive concentration]
Polymer A and polymer B are added to the water system to be treated so that the solid content concentration ratio is polymer A: polymer B = 1: 4 to 4: 1, preferably 1: 2 to 2: 1. The When this use ratio is out of the above range, a good corrosion inhibiting effect cannot be obtained.

また、重合体A及び重合体Bの添加濃度は、処理対象水系の水質や運転状況などを考慮して、十分なスケール抑制効果が得られるような濃度に設定されるが、通常、処理対象水系中の保持濃度(固形分換算濃度)で、重合体Aと重合体Bの合計濃度として1〜500mg/L、特に5〜100mg/Lとなるように連続的に又は間欠的に添加するのが望ましい。   In addition, the addition concentration of the polymer A and the polymer B is set to such a concentration that a sufficient scale suppression effect can be obtained in consideration of the water quality and operating conditions of the treatment target water system. It is added continuously or intermittently so that the total concentration of the polymer A and the polymer B is 1 to 500 mg / L, particularly 5 to 100 mg / L, with the retained concentration (concentration in terms of solid content). desirable.

重合体Aと重合体Bとは、その固形分濃度比及び添加濃度が上記好適範囲内となるように個別に添加しても良く、予め重合体Aと重合体Bとを所定の比率で混合したものを添加しても良い。重合体Aと重合体Bとを個別に添加する場合、これらを同一箇所で添加しても異なる箇所で添加しても良い。   The polymer A and the polymer B may be added individually so that the solid content concentration ratio and the addition concentration are within the above-mentioned preferable range, and the polymer A and the polymer B are mixed in advance at a predetermined ratio. You may add what you did. When polymer A and polymer B are added separately, they may be added at the same location or at different locations.

なお、本発明においては、重合体Aと重合体Bとを処理対象水系に添加した際に得られる各処理効率を妨げない範囲において、他の腐食抑制剤、スケール抑制剤、分散剤、スライムコントロール剤、剥離剤、消泡剤などを併用しても良く、濾過器などの各種水処理機器との併用も可能である。例えば、水系内に銅材質を含む場合には、ベンゾトリアゾールやトリルトリアゾールなどのアゾール類誘導体を併用すれば、銅材質に対する防食性能を向上させることができる。   In the present invention, other corrosion inhibitors, scale inhibitors, dispersants, slime controls are used as long as each treatment efficiency obtained when polymer A and polymer B are added to the water system to be treated is not hindered. An agent, a release agent, an antifoaming agent, and the like may be used in combination, and may be used in combination with various water treatment devices such as a filter. For example, when a copper material is included in the aqueous system, the anticorrosion performance for the copper material can be improved by using an azole derivative such as benzotriazole or tolyltriazole in combination.

[処理対象水系]
本発明の処理対象水系としては、冷却水系が挙げられ、例えば、開放循環式冷却水系等が挙げられる。
[Treatment target water system]
Examples of the water system to be treated of the present invention include a cooling water system such as an open circulation cooling water system.

このような冷却水系では、冷却塔のピットに重合体Aと重合体Bとを添加すれば良い。   In such a cooling water system, the polymer A and the polymer B may be added to the pits of the cooling tower.

以下に実施例及び比較例を挙げて本発明を更に具体的に説明するが、本発明はその要旨を超えない限り、以下の実施例に限定されるものではない。   EXAMPLES The present invention will be described more specifically with reference to examples and comparative examples below, but the present invention is not limited to the following examples unless it exceeds the gist.

実施例1〜5、比較例1〜4
図1に概要を示すベンチスケール冷却水系評価試験装置を用いて、実施例及び比較例の腐食抑制効果を調べる実験を行った。
Examples 1-5, Comparative Examples 1-4
Using the bench scale cooling water system evaluation test apparatus outlined in FIG. 1, an experiment was conducted to investigate the corrosion inhibition effects of the examples and comparative examples.

図1の評価試験装置において、冷却塔1から、ポンプPを有する循環配管2により循環冷却水が熱交換器3に送給され、戻り水が配管4より冷却塔1に戻される。5は補給水の導入配管、6は次亜塩素酸ナトリウム水溶液の導入配管、7は表3に示す評価薬剤の導入配管、8はブロー配管であり、各々ポンプP,P,P,Pを備える。熱交換器3は、外径19mm、長さ1300mm、厚さ2.3mmの炭素鋼製チューブ2本が設けられた蒸気加熱シェル側通水熱交換器である。 In the evaluation test apparatus of FIG. 1, the circulating cooling water is supplied from the cooling tower 1 to the heat exchanger 3 through the circulation pipe 2 having the pump P 1 , and the return water is returned to the cooling tower 1 through the pipe 4. 5 is a supply water introduction pipe, 6 is a sodium hypochlorite aqueous solution introduction pipe, 7 is an introduction pipe for an evaluation agent shown in Table 3, and 8 is a blow pipe. Pumps P 2 , P 3 , P 4 , provided with a P 5. The heat exchanger 3 is a steam heating shell side water flow heat exchanger provided with two carbon steel tubes having an outer diameter of 19 mm, a length of 1300 mm, and a thickness of 2.3 mm.

この評価試験装置の運転条件は次の通りである。
[運転条件]
保有水量:350L
流速:0.1m/秒
熱交換器入口水温:30℃
熱交換器出口水温:35℃(蒸気加熱)
次亜塩素酸ナトリウム添加方法:冷却水の残留塩素濃度が0.3〜0.5mg/Lと
なるように連続注入
評価薬剤添加方法:表2に示す評価薬剤を用い、表3に示す通り、冷却水中の保持濃
度(固形分換算濃度)が20mg/Lとなるように連続注入
The operation conditions of this evaluation test apparatus are as follows.
[Operating conditions]
Retained water volume: 350L
Flow rate: 0.1 m / sec Heat exchanger inlet water temperature: 30 ° C
Heat exchanger outlet water temperature: 35 ° C (steam heating)
Sodium hypochlorite addition method: residual chlorine concentration of cooling water is 0.3 to 0.5 mg / L
As shown in Table 3, the concentration of retention in cooling water is as follows.
Continuous injection so that the concentration (concentration in terms of solid content) is 20 mg / L

市販の初期処理薬剤により初期防食皮膜を形成した炭素鋼製テストチューブを用い、上記の運転を20日間行い、熱交換器チューブに生じた局部腐食の最大深さで腐食抑制効果の評価を行った。20日間の運転後に、熱交換器よりテストチューブを取り出し、チューブの腐食状況(外観)を観察した。インヒビター入り塩酸でテストチューブを酸洗し、腐食生成物を取り除いた。テストチューブ表面に生じた局部腐食深さをデプスゲージで測定し、その最大値を求めた。   Using a carbon steel test tube on which an initial anticorrosion film was formed with a commercially available initial treatment chemical, the above operation was performed for 20 days, and the corrosion inhibition effect was evaluated at the maximum depth of local corrosion that occurred in the heat exchanger tube. . After the operation for 20 days, the test tube was taken out from the heat exchanger, and the corrosion state (appearance) of the tube was observed. The test tube was pickled with hydrochloric acid containing inhibitor to remove corrosion products. The depth of local corrosion occurring on the test tube surface was measured with a depth gauge, and the maximum value was obtained.

試験中の冷却水の平均的水質を表1に、評価薬剤を表2に、試験結果を表3にそれぞれ示す。   Table 1 shows the average water quality of the cooling water during the test, Table 2 shows the evaluation drugs, and Table 3 shows the test results.

Figure 0004244983
Figure 0004244983

Figure 0004244983
Figure 0004244983

Figure 0004244983
Figure 0004244983

表3より明らかなように、本発明の実施例では、比較例に比べ良好な金属の腐食抑制効果を示した。   As is apparent from Table 3, the examples of the present invention showed a better metal corrosion inhibition effect than the comparative examples.

実施例1〜5及び比較例1〜4で用いた冷却水系評価試験装置の概要を示す系統図である。It is a systematic diagram which shows the outline | summary of the cooling water system evaluation test apparatus used in Examples 1-5 and Comparative Examples 1-4.

符号の説明Explanation of symbols

1 冷却塔
2 熱交換器
1 Cooling tower 2 Heat exchanger

Claims (5)

水系の金属の腐食を抑制する方法において、
ランジェリア指数が1.5以上で、かつ[SiO]×[CaH]≧2000(ただし、[SiO]は水中のSiO濃度(mg/L)、[CaH]は水中のCaCOとしてのカルシウム硬度(mg/L))となるように調整された該水系の水に、
マレイン酸及び/又はその水溶性塩から選ばれる1種以上の重合体(以下、「重合体A」と称す。)と、
マレイン酸、無水マレイン酸及びこれらの水溶性塩から選ばれる1種以上と、非イオン性モノエチレン系不飽和単量体の1種以上との共重合体(以下、「重合体B」と称す。)とを添加する金属の腐食抑制方法であって、
重合体Aと重合体Bとを固形分濃度比で重合体A:重合体B=1:4〜4:1の範囲となるように該水系に添加することを特徴とする金属の腐食抑制方法。
In a method for suppressing corrosion of water-based metals,
Langerian index is 1.5 or more, and [SiO 2 ] × [CaH] ≧ 2000 (where [SiO 2 ] is SiO 2 concentration in water (mg / L), [CaH] is CaCO 3 in water The aqueous water adjusted to have a calcium hardness (mg / L))
One or more polymers selected from maleic acid and / or water-soluble salts thereof (hereinafter referred to as “polymer A”);
A copolymer (hereinafter referred to as “polymer B”) of at least one selected from maleic acid, maleic anhydride and water-soluble salts thereof and at least one nonionic monoethylenically unsaturated monomer. )) Is a method for inhibiting corrosion of a metal,
A method for inhibiting corrosion of metal , comprising adding polymer A and polymer B to the aqueous system so that the solid content concentration ratio of polymer A: polymer B = 1: 4 to 4: 1 .
請求項1において、重合体Bの非イオン性モノエチレン系不飽和単量体がイソブチレンであることを特徴とする金属の腐食抑制方法。 Oite to claim 1, a metal process for corrosion inhibition, wherein the non-ionic monoethylenically unsaturated monomer is isobutylene polymer B. 請求項1又は2において、重合体Aと重合体Bとを固形分濃度比で重合体A:重合体B=1:2〜2:1の範囲となるように該水系に添加することを特徴とする金属の腐食抑制方法。3. The polymer according to claim 1, wherein the polymer A and the polymer B are added to the aqueous system so that the ratio of polymer A: polymer B = 1: 2 to 2: 1 in a solid content concentration ratio. A method for inhibiting corrosion of metals. 請求項1ないし3のいずれか1項において、重合体Aの分子量が800〜1500であることを特徴とする金属の腐食抑制方法。The method for inhibiting corrosion of a metal according to any one of claims 1 to 3, wherein the molecular weight of the polymer A is 800 to 1500. 請求項1ないし4のいずれか1項において、重合体Bを構成するマレイン酸成分と非イオン性エチレン成分との合計100モル%に対してマレイン酸成分が25〜75モル%の重合体Bを用いることを特徴とする金属の腐食抑制方法。The polymer B according to any one of claims 1 to 4, wherein the maleic acid component is 25 to 75 mol% with respect to 100 mol% of the total of the maleic acid component and the nonionic ethylene component constituting the polymer B. A method for inhibiting corrosion of a metal, characterized by being used.
JP2005312980A 2005-10-27 2005-10-27 Metal corrosion control method Expired - Fee Related JP4244983B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2005312980A JP4244983B2 (en) 2005-10-27 2005-10-27 Metal corrosion control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2005312980A JP4244983B2 (en) 2005-10-27 2005-10-27 Metal corrosion control method

Publications (2)

Publication Number Publication Date
JP2007119835A JP2007119835A (en) 2007-05-17
JP4244983B2 true JP4244983B2 (en) 2009-03-25

Family

ID=38143979

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2005312980A Expired - Fee Related JP4244983B2 (en) 2005-10-27 2005-10-27 Metal corrosion control method

Country Status (1)

Country Link
JP (1) JP4244983B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009299161A (en) * 2008-06-16 2009-12-24 Kurita Water Ind Ltd Metal corrosion suppression method of water system
JP6113992B2 (en) 2012-10-03 2017-04-12 栗田工業株式会社 Cooling water treatment method

Also Published As

Publication number Publication date
JP2007119835A (en) 2007-05-17

Similar Documents

Publication Publication Date Title
JP4725513B2 (en) Cooling water treatment method
US4298568A (en) Method and composition for inhibiting corrosion of nonferrous metals in contact with water
JP4244983B2 (en) Metal corrosion control method
JP4970674B2 (en) Scale prevention method
JP2008240132A (en) Corrosion inhibitor
JP4923664B2 (en) Scale adhesion inhibitor and cooling water treatment method
US20030173543A1 (en) Organic Corrosion Inhibitors and Corrosion Control Methods for Water Systems
JP6504748B2 (en) Method of inhibiting metal corrosion
JP5559629B2 (en) Water-based metal anticorrosion method
JP4859158B2 (en) Water treatment composition
JP2001137892A (en) Water treating chemical
JP5978711B2 (en) Iron corrosion control method
JP2003082479A (en) Anticorrosive, and corrosion prevention method
JP4277072B2 (en) Boiler corrosion / pitting corrosion inhibitor and corrosion / pitting corrosion prevention method using the same
JP4218673B2 (en) Scale adhesion inhibitor and cooling water treatment method
JP4237454B2 (en) Water-based metal corrosion control method
JP5682727B2 (en) Water treatment method and water treatment agent for cooling water system
JP2004516387A (en) Corrosion inhibition methods suitable for use in drinking water
JP4467046B2 (en) Metal corrosion inhibitor
JP6566010B2 (en) Metal anticorrosive for cooling water and processing method of cooling water system
JP3925296B2 (en) Anticorrosion method
JP4787433B2 (en) Water treatment method
JP6589962B2 (en) Corrosion inhibitor and corrosion prevention method
JP4370488B2 (en) Anticorrosion dispersant and anticorrosion method
JP2009299161A (en) Metal corrosion suppression method of water system

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20080630

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080715

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080827

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20081216

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20081229

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120116

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120116

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130116

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130116

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140116

Year of fee payment: 5

LAPS Cancellation because of no payment of annual fees