JP3401909B2 - Water-based metal corrosion inhibitor - Google Patents

Water-based metal corrosion inhibitor

Info

Publication number
JP3401909B2
JP3401909B2 JP10363394A JP10363394A JP3401909B2 JP 3401909 B2 JP3401909 B2 JP 3401909B2 JP 10363394 A JP10363394 A JP 10363394A JP 10363394 A JP10363394 A JP 10363394A JP 3401909 B2 JP3401909 B2 JP 3401909B2
Authority
JP
Japan
Prior art keywords
water
molecular weight
low molecular
weight polymer
corrosion
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
JP10363394A
Other languages
Japanese (ja)
Other versions
JPH07316848A (en
Inventor
洋 黒部
信博 織田
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 JP10363394A priority Critical patent/JP3401909B2/en
Publication of JPH07316848A publication Critical patent/JPH07316848A/en
Application granted granted Critical
Publication of JP3401909B2 publication Critical patent/JP3401909B2/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
    • C23F11/18Inhibiting 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

Landscapes

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

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
に係り、特に、アニオン交換処理を行って水系におけ
る軟鋼、ステンレス鋼、銅、銅合金などの金属の腐食を
抑制する装置であって、アニオン交換樹脂塔内のスケー
ルの析出を防止して、長期にわたり安定かつ効率的な処
理を継続するための装置に関する。
BACKGROUND OF THE INVENTION The present invention is corrosion inhibition instrumentation metal aqueous
In particular, an apparatus that suppresses corrosion of metals such as mild steel in a water system, stainless steel, copper, and copper alloy by performing anion exchange treatment, and prevents precipitation of scale in the anion exchange resin tower, The present invention relates to a device for continuing stable and efficient processing for a long period of time.

【0002】[0002]

【従来の技術及び先行技術】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。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(C
- )、硫酸イオン(SO4 2- )、硝酸イオン(N
3 -)等により腐食され、孔食を発生させる。そこで、
このような水系と接する金属材の腐食を抑制するため
に、従来、腐食抑制剤として、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を使用する方法がある。
2. Description of the Related Art Open and closed circulating cooling water system,
BACKGROUND ART Mild steel, stainless steel, copper, copper alloys and the like are used as a base material for various devices and pipes used in water systems such as heat storage water systems and closed cold / hot water systems. These base materials used for immersion in water are chlorinated (C
l -), sulfate ion (SO 4 2-), nitrate ion (N
O 3 -) is corroded by such, to generate pitting. Therefore,
In order to suppress the corrosion of the metal material in contact with such an aqueous system, conventionally, as corrosion inhibitors, chromate, molybdate, nitrite, phosphate, phosphonate, zinc salt, benzotriazole, tolyltriazole. , Mercaptobenzothiazole, etc. are available.

【0003】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(特公昭4
8−39704号公報)も提案されている。
Also, a method of treating an aqueous system with an OH type anion exchange resin having chromium ions and zinc ions adsorbed as an anticorrosion agent and eluting the anticorrosion agent in water to prevent corrosion (Japanese Patent Publication No. 4).
No. 8-39704) is also proposed.

【0004】しかしながら、上記腐食抑制剤を含む水を
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。
However, when water containing the above 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.

【0005】このような従来の問題点を解決し、環境汚
染等の問題を引き起こすことなく、水系の金属の腐食を
有効に防止する方法として、本出願人は、先に、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
リマーを添加する方法を提案した(特願平4−3184
38号。以下「先願」という。)。
As a method for solving such conventional problems and effectively preventing corrosion of water-based metals without causing problems such as environmental pollution, the present applicant has previously proposed that water-based corrosive ions A method has been proposed in which the contained water is brought into contact with an anion exchanger carrying an anticorrosive anion, and a low molecular weight polymer is added to the water system (Japanese Patent Application No. 4-3184).
No. 38. Hereinafter referred to as "first application". ).

【0006】即ち、先願の方法は、防食性アニオンであ
るOH- もしくはHCO3 -形に再生されたアニオン交換
樹脂に直接、原水を通水し、腐食性アニオン(Cl-
NO3 -,SO4 2- 等)をイオン交換により除去するもの
である。
That is, according to the method of the prior application, raw water is directly passed through the anion exchange resin regenerated in the form of OH or HCO 3 which is an anticorrosive anion to obtain a corrosive anion (Cl ,
(NO 3 , SO 4 2−, etc.) is removed by ion exchange.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、先願の
方法に従って、硬度成分を含む原水(被処理水)を直
接、アニオン交換樹脂に通水すると、樹脂塔内でスケー
ル(沈殿)が発生する。特に、アニオン交換樹脂のイオ
ン形がOH- 形の場合においては、このスケールの生成
が顕著である。
However, according to the method of the prior application, when raw water containing the hardness component (water to be treated) is directly passed through the anion exchange resin, scale (precipitation) occurs in the resin tower. In particular, when the ionic form of the anion exchange resin is the OH form, the generation of this scale is remarkable.

【0008】このスケールは塩酸や硫酸による樹脂の再
生により除去することはできるが、この場合には再生剤
として防食性アニオンのアルカリ金属塩と鉱酸との2種
類が必要となり、装置的にも操作的にも複雑となる問題
があった。
This scale can be removed by regenerating the resin with hydrochloric acid or sulfuric acid, but in this case, two types of alkali metal salts of anticorrosive anions and mineral acids are required as regenerants, and in terms of equipment. There was a problem that it became complicated in terms of operation.

【0009】一方、鉱酸による再生を実施しないと、強
塩基性アニオン交換樹脂の被処理水中にMgイオンが含
まれている場合(通常の原水にはMg2+が含まれてい
る。)、樹脂塔内でのpH変化によりMgイオンはMg
(OH)2 となって析出し、沈殿を生じ、差圧の上昇に
よりやがて樹脂塔の運転を継続し得なくなる。
On the other hand, in the case where the water to be treated of the strongly basic anion exchange resin contains Mg ions unless regeneration with mineral acid is carried out (normal raw water contains Mg 2+ ). Due to the pH change in the resin tower, Mg ions
(OH) 2 is deposited and precipitates, and due to the rise of the differential pressure, the operation of the resin tower cannot be continued until long.

【0010】本発明は、鉱酸を用いることなくこのよう
なアニオン交換樹脂による処理で水系の金属の腐食を抑
制する装置における樹脂塔内のスケール生成を防止し、
長期にわたり安定かつ効率的な処理を継続することがで
きる水系の金属の腐食抑制装置を提供することを目的と
する。
The present invention prevents scale formation in a resin tower in an apparatus for suppressing corrosion of an aqueous metal by treatment with such an anion exchange resin without using a mineral acid,
It is an object of the present invention to provide a water-based metal corrosion inhibitor capable of continuing stable and efficient treatment for a long period of time.

【0011】[0011]

【課題を解決するための手段】本発明の水系の金属の腐
食抑制装置は、水系の金属の腐食抑制装置であって、該
水系の腐食性イオン含有水又は該水系に供給される腐食
性イオン含有水に低分子量ポリマーを添加する手段と
低分子量ポリマーが添加されたを、防食性アニオン
を担持した強塩基性アニオン交換樹脂と接触させる手段
とを有することを特徴とする。
Corrosion inhibiting system of the metal of the aqueous of the invention To achieve the above object, according to a corrosion inhibiting device for a metallic aqueous corrosive ions supplied to a corrosive ion-containing water or water-based water-based Means for adding a low molecular weight polymer to the contained water,
The low molecular weight polymer is added water, means for creating come in contact with the carrying anticorrosion anionic strong base anion exchange resin
And having .

【0012】以下に本発明を図面を参照して詳細に説明
する。
The present invention will be described below in detail with reference to the drawings.

【0013】図1は本発明の水系の金属の腐食抑制装置
の実施の形態を示す系統図である。
[0013] Figure 1 is a system diagram showing an embodiment of an aqueous metal corrosion inhibiting device <br/> of the present invention.

【0014】本実施例の装置は、貯槽1内のCl- ,S
4 2- ,NO3 -等の腐食性イオン及び硬度成分を含む被
処理水、即ち、水系から抜き出した腐食性イオン含有水
又は水系に供給する腐食性イオン含有水に、配管11よ
り低分子量ポリマーを添加し、低分子量ポリマーが添加
された被処理水を配管12より強塩基性アニオン交換樹
脂塔2に通水して処理し、配管13より流出する処理水
を水系に返送又は供給するものである。
The apparatus of this embodiment is provided with Cl , S in the storage tank 1.
The treated water containing corrosive ions such as O 4 2− and NO 3 and the hardness component, that is, the corrosive ion-containing water extracted from the water system or the corrosive ion-containing water supplied to the water system, has a lower molecular weight than the pipe 11. Water to be treated to which a polymer has been added and a low molecular weight polymer has been added is passed through the pipe 12 to the strongly basic anion exchange resin tower 2 for treatment, and the treated water flowing out from the pipe 13 is returned or supplied to the water system. Is.

【0015】なお、14は強塩基性アニオン交換樹脂の
再生剤の導入配管、15は再生排液の排出配管である。
Reference numeral 14 is a pipe for introducing the regenerant of the strongly basic anion exchange resin, and 15 is a pipe for discharging the regeneration waste liquid.

【0016】本発明において、低分子量ポリマーとして
は、分子量500〜100,000、特に1000〜2
0,000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。
In the present invention, the low molecular weight polymer has a molecular weight of 500 to 100,000, particularly 1000 to 2
A water-soluble polymer of about 10,000, specifically, a maleic acid-isobutylene copolymer, a polyacrylic acid, a partial hydrolyzate of polyacrylamide, an 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, acrylic acid-itaconic acid copolymer, polyitaconic acid, acrylic acid-acrylonitrile copolymer, acrylic acid-vinyl sulfonic acid copolymer, known low molecular weight polymers such as methyl vinyl ether-maleic acid copolymer. To be

【0017】このような低分子量ポリマーの添加量は被
処理水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とする。
The addition amount of such a low molecular weight polymer varies depending on the water quality of the water to be treated, but is usually 0.1 to 500 mg / l with respect to the water to be treated.

【0018】また、低分子量ポリマーを添加した被処理
水を接触させる強塩基性アニオン交換樹脂に担持させる
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し、OH
- ,HCO3 -,CO3 2- 等が挙げられる。従って、本発
明の方法は、強塩基性アニオン交換樹脂として、イオン
形がOH- 形,HCO3 -形又はCO3 2- 形のものを用い
て容易に実施することができる。
Further, the anticorrosion anion carried on the strongly basic anion exchange resin which is brought into contact with the water to be treated to which the low molecular weight polymer is added is dissolved in water by ion exchange even if it does not exhibit anticorrosion, Refers to an anion capable of forming an anticorrosive film by reacting with a dissolved cation in water. OH
-, HCO 3 -, CO 3 2- and the like. Therefore, the method of the present invention can be easily carried out using a strongly basic anion exchange resin having an ionic form of OH form, HCO 3 form or CO 3 2− form.

【0019】低分子量ポリマーを添加した被処理水を防
食性アニオンを担持した強塩基性アニオン交換樹脂と接
触させる方法としては特に制限はないが、一般には、図
1に示す如く、OH- 形,CO3 2- 形又はHCO3 -形の
強塩基性アニオン交換樹脂を充填した充填塔に通水接触
させるのが好ましく、この場合の通水条件等は、被処理
水の水質等に応じて適宜決定される。
[0019] No particular limitation is imposed on the method for contacting with the low molecular weight polymer treatment water corrosion resistance anion loaded with strongly basic anion exchange resin added, but in general, as shown in FIG. 1, OH - form, CO 3 2- form or HCO 3 - is preferable to passed through contact with the strongly basic anion exchange packed column resin was filled in the form, water passing conditions of this case, as appropriate depending on the water quality of the water to be treated It is determined.

【0020】通水を継続することにより、強塩基性アニ
オン交換樹脂のイオン交換性能が低下した場合には、N
aOH,NaHCO3 ,Na2 CO3 等の再生剤で再生
を行う。本発明においては、低分子量ポリマーの作用で
樹脂塔内のスケールの再生が防止されるため、再生剤に
よる再生で強塩基性アニオン交換樹脂は再使用可能とな
り、差圧の上昇等を引き起こすことなく、長期にわたり
繰り返し使用することができる。
If the ion exchange performance of the strongly basic anion exchange resin is lowered by continuing the water flow, N
Regeneration is performed with a regenerant such as aOH, NaHCO 3 , Na 2 CO 3 . In the present invention, since the regeneration of the scale in the resin tower is prevented by the action of the low molecular weight polymer, the strongly basic anion exchange resin can be reused by the regeneration with the regenerant, without causing an increase in the differential pressure. Can be used repeatedly over a long period of time.

【0021】このような本発明の装置は、腐食性イオン
としてCl,SO 2−,NO を含有すると共
に、硬度成分としてMg2+等を含有する水系、例えば
淡水系の金属の腐食抑制に極めて有効である。
[0021] Cl as apparatus, corrosive ions such invention -, SO 4 2-, NO 3 - while containing, aqueous containing Mg 2+, etc. as hardness components, for example corrosion of the freshwater-based metal It is extremely effective for suppression.

【0022】なお、本発明においては、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
止剤等をイオン交換処理水に併用添加してもよい。
In the present invention, if necessary,
Inorganic phosphates (orthophosphates and polymeric phosphates), organic phosphates, phosphonic acids, zinc, nickel salts, tungstates, molybdates, nitrites, borates, silicates, oxycarboxylic acids Corrosion inhibitors such as acid salts, benzotriazole, and mercaptobenzothiazole, scale inhibitors such as lignin derivatives, tannic acids, and polysaccharides such as tempun may be added together with the ion-exchange treated water.

【0023】[0023]

【作用】Cl- ,SO4 2- ,NO3 -等の水中の腐食性イ
オンをCO3 2- ,HCO3 -,OH- 等の防食性アニオン
を担持した強塩基性アニオン交換樹脂と接触させてイオ
ン交換することにより、水中の腐食性イオンはOH-
HCO3 -,CO3 2- 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、水系の腐食性が低減され
る。
Function: Corrosive ions in water such as Cl , SO 4 2− , NO 3 are brought into contact with a strongly basic anion exchange resin carrying anticorrosion anions such as CO 3 2− , HCO 3 , OH −. by ion exchange Te, water corrosive ions OH -,
It is ion-exchanged with anticorrosive anions such as HCO 3 and CO 3 2− , the content thereof is reduced, and the corrosiveness of the water system is reduced.

【0024】このイオン交換に当り、本発明において
は、被処理水に低分子量ポリマーを添加しておくため、
この低分子量ポリマーによるスケール抑制作用により、
樹脂塔内のスケールの生成が防止され、長期間安定かつ
効率的に通水を継続することが可能となる。
In the present invention, since the low molecular weight polymer is added to the water to be treated before the ion exchange,
Due to the scale inhibition effect of this low molecular weight polymer,
Generation of scale in the resin tower is prevented, and stable and efficient water flow can be continued for a long period of time.

【0025】ところで、低分子量ポリマーは、その添加
により、イオン交換で水中に溶出したOH- ,HC
3 -,CO3 2- 等の防食性アニオンや水系由来のC
2+,SiO 2 等の防食性成分の均一な防食皮膜を水系
の金属表面に効果的に形成し、金属の腐食をより一層確
実に抑制するという効果を奏するものであるが、イオン
交換処理前に、被処理水中に添加された低分子量ポリマ
ーは、強塩基性アニオン交換樹脂の腐食性イオンの除去
性能に影響をほとんど及ぼすことなく、また、強塩基性
アニオン交換樹脂に吸着されて水中からほとんど除去さ
れることもない。
By the way, the addition of the low molecular weight polymer
OH eluted in water by ion exchange- , HC
O3 -, CO3 2- Anticorrosive anions such as C and water-derived C
a2+, SiO 2 A water-based anticorrosive film with a uniform anticorrosive component
Effectively forms on the metal surface of the
Although it has the effect of suppressing it, ION
Low molecular weight polymer added to the water to be treated before the exchange treatment
-Removing corrosive ions from strongly basic anion exchange resin
Strongly basic with little effect on performance
Adsorbed on anion exchange resin and almost removed from water
It will not be

【0026】このため、本発明においては、イオン交換
処理水中に、添加された低分子量ポリマーがそのまま移
行し、水系内で上記防食皮膜の形成による防食作用及び
スケール防止作用を有効に発揮する。
Therefore, in the present invention, the added low molecular weight polymer migrates into the ion-exchange treated water as it is, and effectively exhibits the anticorrosive action and scale inhibiting action by forming the anticorrosive film in the water system.

【0027】[0027]

【実施例】以下に実施例及び比較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 more specifically with reference to Examples and Comparative Examples below.

【0028】実施例1 低分子量ポリマーとしてイソブチレン−マレイン酸共重
合体(分子量6,500)を添加した表1に示す水質の
原水1を被処理水として、下記強塩基性アニオン交換樹
脂塔に4リットル/hrの流速で通水した。
Example 1 Raw water 1 of the water quality shown in Table 1 to which an isobutylene-maleic acid copolymer (molecular weight 6,500) was added as a low molecular weight polymer was treated as water to be treated in the following strong basic anion exchange resin tower. Water was passed at a flow rate of liter / hr.

【0029】強塩基性アニオン交換樹脂塔 使用樹脂:ダイヤイオンSA20A(三菱化成(株)
製) 再生レベル:NaOH 66g(CaCO3 換算)/リ
ットル−樹脂 樹脂量:100ml カラム仕様:内径28mm,高さ250mmのガラスカ
ラム イオン交換処理水のCl- 濃度の経時変化、低分子量ポ
リマー濃度の経時変化及びカラム内の差圧の経時変化
を、各々、図2,図3及び図4に示す。なお、強塩基性
アニオン交換樹脂の腐食性アニオンに対するBTC値は
17.2g(CaCO3 換算)/リットル−樹脂であっ
た。
Strongly basic anion exchange resin tower Resin used: Diaion SA20A (Mitsubishi Kasei Co., Ltd.)
Regeneration level: 66 g of NaOH (calculated as CaCO 3 ) / liter-resin resin amount: 100 ml Column specifications: inner diameter 28 mm, height 250 mm glass column ion-exchange treated water Cl concentration change with time, low molecular weight polymer concentration with time. The change and the change over time in the differential pressure in the column are shown in FIGS. 2, 3 and 4, respectively. The BTC value of the strongly basic anion exchange resin with respect to the corrosive anions was 17.2 g (calculated as CaCO 3 ) / liter-resin.

【0030】比較例1 低分子量ポリマーを添加しない表1に示す水質の原水2
について、実施例1と同様に処理した。
Comparative Example 1 Raw water 2 of water quality shown in Table 1 to which a low molecular weight polymer was not added
Was treated in the same manner as in Example 1.

【0031】イオン交換処理水のCl- 濃度の経時変化
及びカラム内の差圧の経時変化を、各々、図5及び図4
に示す。なお、強塩基性アニオン交換樹脂の腐食性アニ
オンに対するBTC値は16.2g(CaCO3 換算)
/リットル−樹脂であった。
The changes in the Cl concentration of the ion-exchange treated water with time and the changes in the differential pressure in the column with time are shown in FIGS. 5 and 4, respectively.
Shown in. The BTC value for the corrosive anion of the strongly basic anion exchange resin is 16.2 g (calculated as CaCO 3 ).
/ Liter-resin.

【0032】[0032]

【表1】 [Table 1]

【0033】図2〜図5の結果から次のことが明らかで
ある。
From the results shown in FIGS. 2 to 5, the following is clear.

【0034】即ち、図2と図5との比較から、低分子量
ポリマーを添加した原水1のイオン交換処理水と低分子
量ポリマーを添加していない原水2のイオン交換処理水
とはほぼ同程度のCl- 濃度の推移を示し、低分子量ポ
リマーの添加は、強塩基性アニオン交換樹脂の腐食性ア
ニオンの除去性能に影響を及ぼさないことが明らかであ
る。
That is, from the comparison between FIG. 2 and FIG. 5, the ion exchange treated water of the raw water 1 to which the low molecular weight polymer was added and the ion exchange treated water of the raw water 2 to which the low molecular weight polymer was not added had almost the same degree. The change in Cl concentration is shown, and it is clear that the addition of the low molecular weight polymer does not affect the ability of the strongly basic anion exchange resin to remove the corrosive anions.

【0035】また、図3より、低分子量ポリマーは通水
初期において樹脂に吸着されるが、しばらくするとイオ
ン交換処理水中の低分子量ポリマー濃度は原水1の低分
子量ポリマー濃度と同等となり、低分子量ポリマーは樹
脂に吸着されることなくイオン交換処理水中にそのまま
移行することが明らかである。
Further, from FIG. 3, the low molecular weight polymer is adsorbed by the resin in the initial stage of water flow, but after a while, the concentration of the low molecular weight polymer in the ion-exchange treated water becomes equal to the concentration of the low molecular weight polymer of the raw water 1, and the low molecular weight polymer is It is clear that is transferred to the ion-exchange treated water without being adsorbed by the resin.

【0036】更に、図5より明らかなように、低分子量
ポリマーを添加した原水1では、カラムの差圧は0.1
kg/cm2 で一定であるが、低分子量ポリマーを添加
していない原水2では、経時的にカラムの差圧が上昇す
る。なお、この原水2を通水したカラム内には、スケー
ルの析出がみられ、この析出物を採取して分析したとこ
ろ、大半がMg(OH)2 であった。この結果から、低
分子量ポリマーの添加により、樹脂塔内のスケール析出
が有効に防止されることが明らかである。
Further, as is clear from FIG. 5, in the raw water 1 to which the low molecular weight polymer was added, the column pressure difference was 0.1.
Although it is constant at kg / cm 2 , in raw water 2 to which the low molecular weight polymer is not added, the differential pressure of the column increases with time. It should be noted that precipitation of scale was observed in the column through which the raw water 2 was passed, and when the precipitate was collected and analyzed, most of it was Mg (OH) 2 . From this result, it is clear that the addition of the low molecular weight polymer effectively prevents the scale deposition in the resin tower.

【0037】[0037]

【発明の効果】以上詳述した通り、本発明の水系の金属
の腐食抑制装置によれば、水系の腐食性イオン含有水又
は水系に供給される腐食性イオン含有水を防食性アニオ
ンを担持した強塩基性アニオン交換樹脂と接触させて腐
食性イオンをイオン交換により除去することにより、水
系の金属の腐食を抑制するにあたり、強塩基性アニオン
交換樹脂塔内におけるスケールの析出を有効に防止し
て、長期にわたり安定かつ効率的なイオン交換処理を行
うことができる。また、低分子量ポリマーの防食皮膜形
成作用で水系内の腐食をより一層確実に防止すると共
に、水系内のスケールの析出をも効果的に防止すること
ができる。
As described above in detail, according to the corrosion inhibiting system of the metal of the water of the present invention, a corrosive ion-containing water supplied to the corrosive ion-containing water or an aqueous water-based carrying anticorrosion anion is removed by ion exchange corrosive ions is contacted with a strongly basic anion exchange resin, per the inhibiting corrosion of aqueous metal, effectively prevent the deposition of scale in a strongly basic anion exchange resin tower Therefore, stable and efficient ion exchange treatment can be performed for a long period of time. In addition, the corrosion-preventing film-forming action of the low-molecular weight polymer can more reliably prevent corrosion in the water system and also effectively prevent precipitation of scale in the water system.

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

【図1】本発明の水系の金属の腐食抑制装置の実施の形
を示す系統図である。
[1] form of implementation of the water-based metal corrosion inhibiting system of the present invention
It is a systematic diagram showing a state .

【図2】実施例1におけるイオン交換処理水のCl-
度の経時変化を示すグラフである。
FIG. 2 is a graph showing the change over time in the Cl concentration of ion-exchange treated water in Example 1.

【図3】実施例1におけるイオン交換処理水の低分子量
ポリマー濃度の経時変化を示すグラフである。
FIG. 3 is a graph showing the change over time in the low molecular weight polymer concentration of ion-exchange treated water in Example 1.

【図4】実施例1及び比較例1におけるカラム内の差圧
の経時変化を示すグラフである。
FIG. 4 is a graph showing changes over time in the differential pressure in the column in Example 1 and Comparative Example 1.

【図5】比較例1におけるイオン交換処理水のCl-
度の経時変化を示すグラフである。
FIG. 5 is a graph showing the change over time in the Cl concentration of ion-exchange treated water in Comparative Example 1.

【符号の説明】[Explanation of symbols]

1 貯槽 2 強塩基性アニオン交換樹脂塔 1 storage tank 2 Strongly basic anion exchange resin tower

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C23F 11/173 C02F 1/42 C02F 5/08 C23F 15/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields surveyed (Int.Cl. 7 , DB name) C23F 11/173 C02F 1/42 C02F 5/08 C23F 15/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水系の金属の腐食抑制装置であって、 水系の腐食性イオン含有水又は該水系に供給される腐
食性イオン含有水に低分子量ポリマーを添加する手段
と、 該低分子量ポリマーが添加されたを、防食性アニオン
を担持した強塩基性アニオン交換樹脂と接触させる手段
とを有することを特徴とする水系の金属の腐食抑制
1. Inhibition of corrosion of water-based metalapparatusAndThe Water containing corrosive ions in water system or spoilage supplied to the water system
Addition of low molecular weight polymer to water containing food ionsMeans to do
When, The low molecular weight polymer was added waterToAnticorrosion anion
Strongly basic anion exchange resinContact withTouchmeans
HaveInhibition of corrosion of water-based metals characterized byDress
Setting.
【請求項2】 請求項1において、水系から抜き出した
腐食性イオン含有水又は水系に供給する腐食性イオン含
有水に、低分子量ポリマーを添加する配管と、低分子量
ポリマーが添加された水が通水される、防食性アニオン
を担持した強塩基性アニオン交換樹脂が充填された充填
塔と、該充填塔から流出する処理水を水系に返送又は供
給する配管とを備えることを特徴とする水系の金属の腐
食抑制装置。
2. The method according to claim 1, which is extracted from the water system.
Containing corrosive ions Containing corrosive ions supplied to water or water system
A pipe for adding low molecular weight polymer to water, and a low molecular weight
Anti-corrosion anion through which water containing polymer is passed
Packed with strong basic anion exchange resin
The tower and the treated water flowing out from the packed tower are returned or supplied to the water system.
A water-based metal corrosion
Food suppression device.
JP10363394A 1994-05-18 1994-05-18 Water-based metal corrosion inhibitor Expired - Fee Related JP3401909B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10363394A JP3401909B2 (en) 1994-05-18 1994-05-18 Water-based metal corrosion inhibitor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10363394A JP3401909B2 (en) 1994-05-18 1994-05-18 Water-based metal corrosion inhibitor

Publications (2)

Publication Number Publication Date
JPH07316848A JPH07316848A (en) 1995-12-05
JP3401909B2 true JP3401909B2 (en) 2003-04-28

Family

ID=14359181

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10363394A Expired - Fee Related JP3401909B2 (en) 1994-05-18 1994-05-18 Water-based metal corrosion inhibitor

Country Status (1)

Country Link
JP (1) JP3401909B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3646385B2 (en) * 1995-12-27 2005-05-11 栗田工業株式会社 Method for inhibiting corrosion of water-based metals
JP4519680B2 (en) * 2005-02-22 2010-08-04 株式会社神戸製鋼所 Accelerated testing method for stress corrosion cracking
DE102014207517A1 (en) * 2013-04-21 2014-12-04 Wieland Kg Corrosion inhibitors, improved color and anti-corrosive coating
FR3023297B1 (en) * 2014-07-02 2021-07-02 Friedrich Wilhelm Wieland CORROSION AND PAINT INHIBITORS
JP6114437B1 (en) * 2016-05-09 2017-04-12 新菱冷熱工業株式会社 Corrosive anion removing apparatus and method for regenerating anion exchange resin

Also Published As

Publication number Publication date
JPH07316848A (en) 1995-12-05

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