JPH03277790A - Method for preventing corrosion of boiler - Google Patents

Method for preventing corrosion of boiler

Info

Publication number
JPH03277790A
JPH03277790A JP7674790A JP7674790A JPH03277790A JP H03277790 A JPH03277790 A JP H03277790A JP 7674790 A JP7674790 A JP 7674790A JP 7674790 A JP7674790 A JP 7674790A JP H03277790 A JPH03277790 A JP H03277790A
Authority
JP
Japan
Prior art keywords
boiler
acid
salt
water
compound
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.)
Pending
Application number
JP7674790A
Other languages
Japanese (ja)
Inventor
Shunichi Akama
俊一 赤間
Masayo Ito
雅代 伊藤
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.)
AKUASU KK
Original Assignee
AKUASU KK
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 AKUASU KK filed Critical AKUASU KK
Priority to JP7674790A priority Critical patent/JPH03277790A/en
Publication of JPH03277790A publication Critical patent/JPH03277790A/en
Pending legal-status Critical Current

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  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Abstract

PURPOSE:To effectively prevent the corrosion of a boiler operated or stopped by incorporating a compd. forming tin ion in water, an org. compd. such as erythorbic acid and an aliphatic hydroxycarboxylic acid in the boiler water respectively in a specified concn. CONSTITUTION:From 10 to 200mg Sn/l of a compd. (a) generating tin ion or tin complex ion in water, 5-300mg/l of <=1 kind of org. compd. or its salt (b) among erythorbic acid, ascorbic acid, sorbic acid, gallic acid and catechol and 30-100mg/l of an aliphatic hydroxycarboxylic acid or its salt (c) are incorporated in the boiler water. Stannous chloride is preferably used as the compd. (a). Gluconic acid or its salt and/or citric acid or its salt are preferably used as the salt (c). The corrosion of the boiler operated or stopped is prevented, and the boiler is again operated as such after stoppage.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はボイラの防食方法、とくにボイラの稼働中のみ
ならず、稼働停止中にも有効なボイラの防食方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a boiler corrosion prevention method, and particularly to a boiler corrosion prevention method that is effective not only when the boiler is in operation but also when the boiler is stopped.

〔従来技術〕[Prior art]

ボイラを防食する方法として、モリブデン化合物、脂肪
族オキシカルボン酸、無機重金属化合物などを組み合わ
せてボイラ水中に添加する方法(特公昭62−2715
7号)やボイラ水系の2価のスズ濃度とpHを適当な範
囲にコントロールする方法(特開昭64−73093号
)などが知られている。しかしこれら従来の方法はボイ
ラ停止時の防食効果に乏しく、実際のボイラ水系に適用
し難いという欠点があった。すなわち、一般にボイラは
発生蒸気の使用状況に応じて稼働−停止が繰り返される
ものであるが、ボイラの設置台数や運転方法により稼働
−停止のサイクルが数日間〜数週間に及ぶこともしばし
ばである。ところが前記防食方法では、ボイラが稼働状
態(すなわち高温状態)にあるときは有効であっても、
稼働停止時に水温が低下すると防食性が弱くなるので、
ボイラ内の防食の為に蒸気が必要ない場合にもボイラを
高温状態に維持したり、あるいは停止させるにしても停
止時には他の防食手段(例えば、ヒドラジンや亜硫酸塩
のようないわゆる脱酸素剤を高濃度にボイラ水系に添加
するなど)を併せて講じなければならず、再稼働に入る
ときには再びボイラ水を稼働時用の防食剤入りのものに
交換するなどの必要があり、運転作業を煩雑にするばか
りか、ランニングコストも増大してしまうという問題点
があった。
As a method for preventing corrosion of boilers, a method of adding a combination of molybdenum compounds, aliphatic oxycarboxylic acids, inorganic heavy metal compounds, etc. to boiler water (Japanese Patent Publication No. 62-2715
7) and a method of controlling the divalent tin concentration and pH of the boiler water system within an appropriate range (Japanese Patent Application Laid-open No. 73093/1983). However, these conventional methods have the disadvantage that they have poor corrosion protection effect when the boiler is stopped and are difficult to apply to actual boiler water systems. In other words, boilers are generally operated and stopped repeatedly depending on the usage status of the generated steam, but depending on the number of boilers installed and the operating method, the cycle of operation and stopping can often extend from several days to several weeks. . However, although the above corrosion prevention method is effective when the boiler is in operation (i.e., in a high temperature state),
Corrosion resistance weakens when the water temperature drops when the product is stopped, so
Even if steam is not needed to prevent corrosion inside the boiler, the boiler may be maintained at a high temperature, or even if the boiler is shut down, other corrosion protection measures (for example, so-called oxygen scavengers such as hydrazine or sulfite) may be used when the boiler is shut down. (e.g., adding a high concentration to the boiler water system), and when restarting operations, it is necessary to replace the boiler water with one containing anticorrosive agent for use during operation, which complicates operation work. There was a problem in that not only was the running cost increased, but the running cost also increased.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

そこで本発明は、ボイラ稼働中は勿論のこと、ボイラ停
止に際しても何隻追加的な手段を講することなくそのま
まで防食効果が発揮でき、またそのまま再稼働に入って
も何隻支障を生じないボイラ防食方法を提供しようとす
るものである。
Therefore, the present invention can exert its anticorrosion effect not only while the boiler is in operation, but also when the boiler is stopped without any additional measures, and even if the boiler is restarted without any problems. The present invention aims to provide a boiler corrosion prevention method.

〔課題を解決するための手段〕 本発明者らは、上記の目的を達成するために鋭意研究を
進めた結果、ボイラ水系に、水中でスズイオンまたはス
ズの錯イオンを生成する化合物とある特定の有機化合物
を組み合わせて添加することにより、ボイラが稼働状態
にあるかあるいは停止状態にあるかにかかわらず、ボイ
ラ内鋼材表面を良好に防食することができることを見出
した。
[Means for Solving the Problems] As a result of intensive research to achieve the above object, the present inventors added a certain specific compound to the boiler water system that produces tin ions or tin complex ions in water. It has been found that by adding a combination of organic compounds, the surface of the steel material inside the boiler can be well protected against corrosion regardless of whether the boiler is in operation or stopped.

すなわち本発明は、ボイラ水中に、水中でスズイオンま
たはスズの錯イオンを生成する化合物(a)を10〜2
00■Sn/ j! 、エリソルビン酸、アスコルビン
酸、ソルビン酸、没食子酸及びカテコールより選ばれる
1種以上の有機化合物またはその塩からなる化合物(b
)を5〜300■/l、および脂肪族オキシカルボン酸
またはその塩からなる化合物(c)を30〜1000■
/l存在させることを特徴とするボイラ防食方法である
That is, the present invention contains 10 to 2 of the compound (a) that produces tin ions or tin complex ions in boiler water.
00■Sn/j! , erythorbic acid, ascorbic acid, sorbic acid, gallic acid, and catechol.
) of 5 to 300 ■/l, and compound (c) consisting of an aliphatic oxycarboxylic acid or its salt at 30 to 1000 ■/l.
This is a method for preventing corrosion of a boiler, characterized in that the boiler corrosion prevention method is characterized by causing the presence of

本発明において用いられる化合物(a)としては、たと
えば塩化第1スズ、硫酸第1スズなどのスズの無機酸塩
や酢酸スズなどのスズの有機酸塩、たとえばスズ酸ナト
リウム、亜スズ酸カリウムなどのスズ酸化合物や亜スズ
酸化合物等、水中でスズイオン又はスズの錯イオンを生
成する化合物が挙げられる。
Examples of the compound (a) used in the present invention include inorganic salts of tin such as stannous chloride and stannous sulfate, organic salts of tin such as tin acetate, sodium stannate, potassium stannite, etc. Examples include compounds that generate tin ions or tin complex ions in water, such as stannic acid compounds and stannous acid compounds.

また本発明において用いられる化合物(c)としては、
グリコール酸、酒石酸、乳酸、クエン酸、リンゴ酸など
の脂肪族オキシカルボン酸、又はこれらのアルカリ金属
塩などが挙げられる。
In addition, the compound (c) used in the present invention includes:
Examples include aliphatic oxycarboxylic acids such as glycolic acid, tartaric acid, lactic acid, citric acid, and malic acid, and alkali metal salts thereof.

本発明における防食機構は明らかでないが、化合物(a
)が存在しないかまたは存在しても濃度が低い場合には
、稼働時および停止時共に防食効果を得る事ができない
。また、化合物(c)が存在しないかまたは存在しても
濃度が低い場合には、化合物(a)の濃度やボイラ水系
のpHなどにより、稼働停止にかかわらず防食性能が発
揮できない場合がある。また、化合物(′b)が存在し
ないかまたは存在しても濃度が低い場合には、全般に防
食性能が低下する傾向があるが、特にボイラ停止時にお
ける防食性能低下が顕著である。以上の通り3成分のう
ち1成分でも存在しないかまたは存在しても濃度が低い
場合には、前記問題点を解決することができない。また
、各々の成分を前記の範囲をこえる濃度で存在させても
、防食効果の向上は望めず、ランニングコストが増大す
るだけで実用的でない。
Although the anticorrosion mechanism in the present invention is not clear, the compound (a
) does not exist, or even if it does exist, the concentration is low, no anticorrosion effect can be obtained both during operation and when stopped. Furthermore, if the compound (c) is not present or is present but at a low concentration, the anticorrosion performance may not be exhibited regardless of the operation stoppage, depending on the concentration of the compound (a) and the pH of the boiler water system. Further, if compound ('b) is not present or is present but at a low concentration, there is a tendency for the anticorrosion performance to deteriorate overall, and the deterioration in the anticorrosion performance is particularly noticeable when the boiler is stopped. As mentioned above, if even one of the three components is absent, or even if it is present, the concentration is low, the above problems cannot be solved. Further, even if each component is present in a concentration exceeding the above range, no improvement in anticorrosion effect can be expected, and running costs only increase, which is impractical.

さらに本発明においては、本発明の効果を損わない限り
、他の防食剤、スケール防止剤、復水処理剤等を併用す
ることができる。かかる薬剤としては、ヒドラジン、亜
硫酸塩、リン酸塩、ホスホン酸化合物、揮発性アミン、
ポリアクリル酸などの水溶性有機高分子化合物などが挙
げられる。
Furthermore, in the present invention, other anticorrosive agents, scale inhibitors, condensate treatment agents, etc. can be used in combination as long as the effects of the present invention are not impaired. Such agents include hydrazine, sulfites, phosphates, phosphonic acid compounds, volatile amines,
Examples include water-soluble organic polymer compounds such as polyacrylic acid.

〔実施例1〕 電熱式ヒーター(伝熱面積0.335M)が水中に浸漬
している保有水量2.5I!のオートクレーブ装置を、
給水および表1に示す割合で薬剤を補給しながら蒸気圧
8 kgf/cd、蒸気発生量2.5 kg/ hにて
稼働し、10倍濃縮のオートクレーブ内保有水(ボイラ
水)を得た。次に、ヒーターをボイラ用鋼管(STB4
2)製のものに交換し、引き続きブロー率10%で、表
1に示す割合で薬剤を含む給水を連続的に補給しながら
蒸気圧8kgf/CIA、蒸気発生12.5kg/hで
4時間運転したのち稼働を停止し、蓋を開放したまま水
温を60℃に保持して翌日まで放置した。次の日には再
び同様な運転を繰返し、このようにして4日間運転を行
った後ヒーターに生じたピッチング数を計数した。その
結果を表1に合わせて示した。
[Example 1] An electric heater (heat transfer area: 0.335M) is immersed in water and holds 2.5 I of water! autoclave equipment,
The autoclave was operated at a steam pressure of 8 kgf/cd and a steam generation rate of 2.5 kg/h while supplying water and chemicals at the rates shown in Table 1 to obtain 10 times concentrated water (boiler water) in the autoclave. Next, install the heater into a boiler steel tube (STB4).
2), and continued to operate for 4 hours at a blow rate of 10%, a steam pressure of 8 kgf/CIA, and a steam generation of 12.5 kg/h while continuously replenishing water containing chemicals at the ratio shown in Table 1. Thereafter, the operation was stopped, and the water temperature was maintained at 60° C. with the lid open until the next day. On the next day, the same operation was repeated again, and after 4 days of operation in this manner, the number of pittings that occurred in the heater was counted. The results are shown in Table 1.

なお、実験に用いた給水の水質は下記のとおりである。The quality of the water supply used in the experiment is as follows.

胎1(K! pH・          7.4 電気伝導率(μ5101):    780塩化物イオ
ンCI (■ムe):  200全硬度(* CaC0
z/ l )  :    1未満M −フルbり度 
C■ CaC0z/ 1 ):    4 4シリカ(
■5iOz/1’)  :     23全鉄(+qr
 Fe/jり    ・0.05未満表 隘 (■Sn/7り (■/l’) (■/7り ES: 0 #:30 GA: 0 GL : 450 〃:150 〃:150 ”:150 ES : 300 〃:120 〃:450 :対照方法 ES:エリソルビン酸ナトリウム GA:没食子酸ナトリウム GLニゲルコン酸ナトリウム 〔実施例2〕 有効容積lI!のポリ容器に下記のような水質に調整し
た大工ボイラ水および表2に示す割合で薬剤を入れ、恒
温槽中で水温60℃にした後、151×40WM×2M
Mの軟鋼板をボイラ水中に浸漬するように吊して取り付
けた。密閉状態にして恒温槽中で水温60℃に維持しな
がら30日間放置した。テスト終了後、テストピースを
取り出して減量を測定し、腐食度(a+dd)を算出し
た。その結果を表2に合わせて示した。
Womb 1 (K! pH 7.4 Electrical conductivity (μ5101): 780 Chloride ion CI (■mue): 200 Total hardness (*CaC0
z/l): less than 1 M - full brittleness
C ■ CaC0z/ 1 ): 4 4 silica (
■5iOz/1'): 23 total iron (+qr
Fe/jri ・Less than 0.05 (■Sn/7ri (■/l') (■/7ri ES: 0 #:30 GA: 0 GL: 450 〃:150 〃:150 '':150 ES : 300 〃: 120 〃: 450 : Control method ES: Sodium erythorbate GA: Sodium gallate GL Sodium nigerconate [Example 2] Carpenter boiler water adjusted to the following water quality and Add the chemicals in the proportions shown in Table 2, raise the water temperature to 60℃ in a constant temperature bath, and then
A mild steel plate of size M was hung and attached so as to be immersed in boiler water. It was left in a sealed state for 30 days while maintaining the water temperature at 60° C. in a constant temperature bath. After the test was completed, the test piece was taken out, the weight loss was measured, and the degree of corrosion (a+dd) was calculated. The results are shown in Table 2.

兆盃立水水l pH・         11.8 電気伝導率(μs/cm)   :   5430全硬
度(W CaC0z/ I! )  :    1未満
P −アル方り度 (■CaC0:+/ jり  : 
 1 1 0 0塩化物イオン(■C1/l):   
600硫酸イオン(■S04/l) :   100シ
リカ(■5iOz/jり   :    250全鉄(
■Fe/l )           0.05未満 表 ES : 120 〃:60 〃:30 〃:15 〃:3 〃:30 〃:300 SB:30 〃:3 〃300 GA :  30 〃:120 AS:30 C^:30 〃:60 〃:30 〃:450 ”:450 〃:450 〃:450 〃:450 CT : 450 *:対象方法 ES:エリソルビン酸ナトリウム SB:ソルビン酸カリウム GA:没食子酸ナトリウム AS:アスコルビン酸ナトリウム CA:カテコール GLニゲルコン酸ナトリウム CT:クエン酸カリウム 〔発明の効果〕 本発明のボイラ防食方法によれば、ボイラ稼働時に用い
た防食剤を含むボイラ水を交換することなく、そのまま
運転を停止しても有効にボイラが防食され、再運転に際
してもボイラ水を交換する必要がない。従ってボイラの
稼働−停止の作業が極めて容易であり、水処理薬剤の使
用量も低減できて経済的でもある。
Chokatachisui water l pH・11.8 Electrical conductivity (μs/cm): 5430 Total hardness (W CaC0z/I!): Less than 1 P-Al straightness (■CaC0:+/J):
1 1 0 0 chloride ion (■C1/l):
600 sulfate ion (■S04/l): 100 silica (■5iOz/jri: 250 total iron (
■Fe/l) Less than 0.05 ES: 120 〃:60 〃:30 〃:15 〃:3 〃:30 〃:300 SB:30 〃:3 〃300 GA: 30 〃:120 AS: 30 C^ :30 〃:60 〃:30 〃:450 ”:450 〃:450 〃:450 〃:450 CT: 450 *: Target method ES: Sodium erythorbate SB: Potassium sorbate GA: Sodium gallate AS: Sodium ascorbate CA: Catechol GL Sodium nigerconate CT: Potassium citrate [Effects of the invention] According to the boiler corrosion prevention method of the present invention, the boiler operation can be stopped without replacing the boiler water containing the anticorrosion agent used during boiler operation. The boiler is also effectively protected from corrosion, and there is no need to replace the boiler water when restarting the boiler.Therefore, it is extremely easy to start and stop the boiler, and the amount of water treatment chemicals used can be reduced, making it economical.

Claims (3)

【特許請求の範囲】[Claims] (1)ボイラ水中に、水中でスズイオンまたはスズの錯
イオンを生成する化合物(a)を10〜200mgSn
/l、エリソルビン酸、アスコルビン酸、ソルビン酸、
没食子酸及びカテコールより選ばれる1種以上の有機化
合物またはその塩からなる化合物(b)を5〜300m
g/l、および脂肪族オキシカルボン酸またはその塩か
らなる化合物(c)を30〜1000mg/l存在させ
ることを特徴とするボイラ防食方法。
(1) Add 10 to 200 mg of the compound (a) that produces tin ions or tin complex ions in boiler water.
/l, erythorbic acid, ascorbic acid, sorbic acid,
5 to 300 m of compound (b) consisting of one or more organic compounds selected from gallic acid and catechol or a salt thereof
g/l, and a compound (c) consisting of an aliphatic oxycarboxylic acid or a salt thereof in an amount of 30 to 1000 mg/l.
(2)化合物(a)が塩化第1スズである特許請求の範
囲第1項記載のボイラ防食方法。
(2) The boiler corrosion prevention method according to claim 1, wherein the compound (a) is stannous chloride.
(3)化合物(c)がグルコン酸またはその塩、および
/またはクエン酸またはその塩である特許請求の範囲第
1項記載のボイラ防食方法。
(3) The boiler corrosion protection method according to claim 1, wherein the compound (c) is gluconic acid or a salt thereof, and/or citric acid or a salt thereof.
JP7674790A 1990-03-28 1990-03-28 Method for preventing corrosion of boiler Pending JPH03277790A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7674790A JPH03277790A (en) 1990-03-28 1990-03-28 Method for preventing corrosion of boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7674790A JPH03277790A (en) 1990-03-28 1990-03-28 Method for preventing corrosion of boiler

Publications (1)

Publication Number Publication Date
JPH03277790A true JPH03277790A (en) 1991-12-09

Family

ID=13614197

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7674790A Pending JPH03277790A (en) 1990-03-28 1990-03-28 Method for preventing corrosion of boiler

Country Status (1)

Country Link
JP (1) JPH03277790A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997028291A1 (en) * 1996-02-05 1997-08-07 Nippon Steel Corporation Surface-treated metallic material with corrosion resistance and surface treatment used therefor
US6190780B1 (en) 1996-02-05 2001-02-20 Nippon Steel Corporation Surface treated metal material and surface treating agent
WO2006047766A1 (en) * 2004-10-27 2006-05-04 A.S. Inc. Corrosion inhibition method for use in recirculating cooling water systems
JP2006150267A (en) * 2004-11-30 2006-06-15 Aquas Corp Boiler water treating agent and method for treating boiler water by using the same
WO2007014362A1 (en) * 2005-07-27 2007-02-01 A.S. Incorporated Corrosion inhibition method for use in boiler water systems
JP2008248357A (en) * 2007-03-30 2008-10-16 Aquas Corp Boiler treating agent composition and corrosion prevention method of boiler system
CN102634803A (en) * 2012-04-18 2012-08-15 山西太钢不锈钢股份有限公司 Long-period shutdown protection method for generator sets
US20120282136A1 (en) * 2011-05-06 2012-11-08 John Richardson Methods and compositions for inhibiting metal corrosion in heated aqueous solutions

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997028291A1 (en) * 1996-02-05 1997-08-07 Nippon Steel Corporation Surface-treated metallic material with corrosion resistance and surface treatment used therefor
US6190780B1 (en) 1996-02-05 2001-02-20 Nippon Steel Corporation Surface treated metal material and surface treating agent
WO2006047766A1 (en) * 2004-10-27 2006-05-04 A.S. Inc. Corrosion inhibition method for use in recirculating cooling water systems
JP2006150267A (en) * 2004-11-30 2006-06-15 Aquas Corp Boiler water treating agent and method for treating boiler water by using the same
JP4718823B2 (en) * 2004-11-30 2011-07-06 アクアス株式会社 Boiler water treatment agent and boiler water treatment method using the same
WO2007014362A1 (en) * 2005-07-27 2007-02-01 A.S. Incorporated Corrosion inhibition method for use in boiler water systems
JP2008248357A (en) * 2007-03-30 2008-10-16 Aquas Corp Boiler treating agent composition and corrosion prevention method of boiler system
US20120282136A1 (en) * 2011-05-06 2012-11-08 John Richardson Methods and compositions for inhibiting metal corrosion in heated aqueous solutions
US9115432B2 (en) * 2011-05-06 2015-08-25 Chemtreat, Inc. Methods and compositions for inhibiting metal corrosion in heated aqueous solutions
CN102634803A (en) * 2012-04-18 2012-08-15 山西太钢不锈钢股份有限公司 Long-period shutdown protection method for generator sets

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