JPH04166298A - Water treating agent - Google Patents
Water treating agentInfo
- Publication number
- JPH04166298A JPH04166298A JP29315690A JP29315690A JPH04166298A JP H04166298 A JPH04166298 A JP H04166298A JP 29315690 A JP29315690 A JP 29315690A JP 29315690 A JP29315690 A JP 29315690A JP H04166298 A JPH04166298 A JP H04166298A
- Authority
- JP
- Japan
- Prior art keywords
- water
- acid
- scale
- present
- 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.)
- Pending
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- Preventing Corrosion Or Incrustation Of Metals (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、水系における金属の腐食やスケール生成を防
止することが出来るスケール防止剤、腐食防止剤等の水
処理剤に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to water treatment agents such as scale inhibitors and corrosion inhibitors that can prevent metal corrosion and scale formation in water systems.
〔従来の技術及び発明が解決しようとする課題〕一般に
、石油精製プラント、化学工業プラント、空調プラント
等の冷却水系及びボイラー水系においては、金属管表面
や水路壁面、ボイラーの伝熱面等に腐食やスケールが生
成し、効率低下を招(たけてな(、閉塞事故をも引き起
こしかねず、常に腐食やスケールの生成を防止するよう
に細心の注意が払われている。[Prior art and problems to be solved by the invention] In general, in cooling water systems and boiler water systems of oil refining plants, chemical industry plants, air conditioning plants, etc., corrosion occurs on the surfaces of metal pipes, waterway walls, heat transfer surfaces of boilers, etc. This can lead to the formation of corrosion and scale, which can reduce efficiency and even cause blockages, so great care is always taken to prevent corrosion and scale formation.
従来、このような水系に対し、例えばスケールを防止す
るためにポリアクリル酸塩、ポリマレイン酸、リン酸系
化合物が通用されている。Conventionally, polyacrylates, polymaleic acids, and phosphoric acid-based compounds have been used in such aqueous systems to prevent scale, for example.
しかし、スケール防止剤として、例えばポリアクリル酸
塩を用いるとカルシウム硬度が高い高硬度水系において
は、水中のカルシウムイオンと反応して不溶性塩を形成
し、スケール防止能が低下するばかりでなく、スケール
の発生原因となる場合すらある。However, when using polyacrylate as a scale inhibitor, for example, in highly hard water systems with high calcium hardness, it not only reacts with calcium ions in the water to form insoluble salts, but also reduces scale prevention ability. In some cases, it may even cause the occurrence of
またマレイン酸単独重合物あるいは共重合物は水処理剤
として使用した場合、スケール抑制効果は優れているが
、腐食抑制剤としての効果は十分でない等の欠点を有す
る。Furthermore, when used as a water treatment agent, a maleic acid homopolymer or copolymer has an excellent scale inhibiting effect, but has drawbacks such as an insufficient effect as a corrosion inhibitor.
一方、前記の水系における金属の腐食防止のためには、
クロム酸塩やリン酸塩が用いられてきた。しかし、クロ
ム酸塩はその毒性のために排出規制の対象となっている
。また、リン酸塩についても閉鎖水域における富栄養化
の原因となるため規制の動向が顕著になりつつある。On the other hand, in order to prevent metal corrosion in the water system mentioned above,
Chromates and phosphates have been used. However, chromate is subject to emission regulations due to its toxicity. Additionally, there is a growing trend towards regulation of phosphates as they cause eutrophication in closed water bodies.
本発明者らは、かかる従来の課題を解決すべく鋭意研究
の結果、ポリエポキシコハク酸又はその塩が特にスケー
ル抑制剤、腐食抑制側として優れた性能を有する事を見
出し、本発明を完成するに至った。As a result of intensive research to solve such conventional problems, the present inventors discovered that polyepoxysuccinic acid or its salt has excellent performance particularly as a scale inhibitor and corrosion inhibitor, and completed the present invention. reached.
即ち、本発明は、次式
%式%(1)
c式中、nは2〜40の整数を表し、X、 Yは水素原
子、−価若しくは二価の金属陽イオン、アンモニウムイ
オン又は有機アミン陽イオンを表す。〕で示されるポリ
エポキシコハク酸又はその塩からなることを特徴とする
水処理剤を提供するものである。That is, the present invention is based on the following formula % formula % (1) c where n represents an integer of 2 to 40, and Represents a cation. ] The present invention provides a water treatment agent characterized by comprising polyepoxysuccinic acid or a salt thereof.
本発明の前記一般式(1)で表されるポリエポキシコハ
ク酸又はその塩は従来公知の方法によって得ることがで
きる。The polyepoxysuccinic acid or its salt represented by the general formula (1) of the present invention can be obtained by a conventionally known method.
例えば、タングステン酸ナトリウムを触媒として、過酸
化水素にてマレイン酸塩をエポキシ化してエポキシコハ
ク酸塩とする(G、B、Payne。For example, maleate is epoxidized with hydrogen peroxide using sodium tungstate as a catalyst to give epoxysuccinate (G, B, Payne).
P、H,Williams、 J、Org、Chem、
、 24.54 (’59))。P, H, Williams, J, Org, Chem.
, 24.54 ('59)).
次にエポキシコハク酸塩をメチルあるいはエチルエステ
ルとした後、無溶剤系あるいは不活性溶剤中にて開環重
合し、得られた重合体を加水分解することにより、前記
一般式(1)で表されるポリエポキシコハク酸が得られ
る。更にこのポリエポキシコハク酸は、1価金属陽イオ
ン、2価金属陽イオン、アンモニウムイオン又は有機ア
ミン陽イオンによりカルボン酸基の一部又は全てを塩の
形に変えてもよい。Next, after converting the epoxy succinate into a methyl or ethyl ester, ring-opening polymerization is performed in a solvent-free system or in an inert solvent, and the resulting polymer is hydrolyzed to form a compound represented by the general formula (1). Polyepoxysuccinic acid is obtained. Further, in this polyepoxysuccinic acid, some or all of the carboxylic acid groups may be converted into a salt form using a monovalent metal cation, a divalent metal cation, an ammonium ion, or an organic amine cation.
本発明の水処理剤は、純水、軟水、水道水及び工業用水
等あらゆる水質に適用でき、使用濃度は、目的に応じて
決定されるものであるが、一般には有効成分として0.
1〜500pp1mであり、特に0.5〜200ppm
であることが好ましい。また、対象水系のpH範囲は特
に制限はないが、一般にpH6〜14であり、好ましく
はpF16〜12である。The water treatment agent of the present invention can be applied to all types of water such as pure water, soft water, tap water, and industrial water, and the concentration used is determined depending on the purpose, but generally the active ingredient is 0.
1 to 500 ppm, especially 0.5 to 200 ppm
It is preferable that Further, the pH range of the target aqueous system is not particularly limited, but it is generally pH 6 to 14, preferably pF 16 to 12.
本発明の水処理剤の対象水系の具体例としては、ボイラ
ー水系や開放又は密閉循環式冷却水系、−過式冷却水系
、ブライン水系、一部の転炉集塵水系、高炉転炉等のド
ライピットの冷却水系、コークス工場等におけるアンモ
ニア蒸留塔水系、都市ゴミ清掃工場等の焼却灰水系、海
水脱塩装置等が挙げられる。Specific examples of target water systems for the water treatment agent of the present invention include boiler water systems, open or closed circulation cooling water systems, overflow cooling water systems, brine water systems, some converter dust collection water systems, and dry water systems such as blast furnace converters. Examples include cooling water systems in pits, ammonia distillation tower water systems in coke factories, etc., incineration ash water systems in municipal waste cleaning plants, and seawater desalination equipment.
本発明の水処理剤は、単独で使用して効果を発揮するも
のであるが、従来水処理剤として使用されている薬剤、
例えば防錆剤、他の防食剤、あるいはキレート剤、分散
剤等を併用することも可能である。The water treatment agent of the present invention is effective when used alone, but it can also be used with agents conventionally used as water treatment agents,
For example, it is also possible to use a rust preventive agent, another anticorrosive agent, a chelating agent, a dispersant, etc. in combination.
併用する薬剤としては、アミン、イミダシリン、アミド
などのN含有化合物、リン酸エステル、ヒドロキシカル
ボン酸類、リグニンスルホン酸塩、芳香族スルホン酸の
ホルマリン縮合物(塩)、メラミンスルホン酸ホルマリ
ン縮合物(塩)、アクリル酸又はメタクリル酸系のポリ
マー(ポリカルボン酸)、オレフィンとマレイン酸の共
重合物、亜硝酸塩、硫酸塩、リン酸塩などの無機塩類、
芳香族カルボン酸塩、脂肪族カルボン酸塩、アミノポリ
カルボン酸塩、千オ尿素、スルホコハク酸類、ポリエチ
レングリコール、チオグリコール酸エステル、ポリエチ
レンイミン、ポリエチレンイミド、ヘンゾトリアヅール
などが挙げられる。Concomitant drugs include amines, imidacillin, N-containing compounds such as amides, phosphoric acid esters, hydroxycarboxylic acids, lignin sulfonates, formalin condensates of aromatic sulfonic acids (salts), melamine sulfonic acid formalin condensates (salts), etc. ), acrylic acid or methacrylic acid polymers (polycarboxylic acids), copolymers of olefin and maleic acid, inorganic salts such as nitrites, sulfates, and phosphates,
Examples include aromatic carboxylic acid salts, aliphatic carboxylic acid salts, aminopolycarboxylic acid salts, 1,000 urea, sulfosuccinic acids, polyethylene glycol, thioglycolic acid esters, polyethyleneimine, polyethyleneimide, and henzotriadur.
本発明の水処理剤は、分子内にエーテル基及びカルボキ
シル基を多量に持つため、スケールや管壁等への吸着性
が向上する。従って、スケール防止能、腐食抑制能が向
上すると共に、毒性、生分解性にも優れているため、環
境に対する悪影響も少ないという特長を持つ。Since the water treatment agent of the present invention has a large amount of ether groups and carboxyl groups in its molecules, its adsorption to scales, pipe walls, etc. is improved. Therefore, it has improved scale prevention ability and corrosion inhibition ability, and is also excellent in toxicity and biodegradability, so it has the advantage of having little negative impact on the environment.
以下、合成例及び実施例において、本発明を更に具体的
に説明するが、本発明はこれらの実施例に限定されるも
のではない。Hereinafter, the present invention will be explained in more detail with reference to Synthesis Examples and Examples, but the present invention is not limited to these Examples.
尚、本発明の効果を示す尺度としてはスケール抑制、腐
食抑制を採用した。Incidentally, scale inhibition and corrosion inhibition were adopted as measures showing the effects of the present invention.
ポリエポキシコハク酸塩の合成例
Payne ら(J、Org、Chem、、 2A、
54(’59))の方法に従いエポキシコハク酸塩を合
成した。Synthesis example of polyepoxy succinate Payne et al. (J, Org, Chem, 2A,
Epoxy succinate was synthesized according to the method of 54 ('59)).
即ち、温度計、攪拌機、滴下ロート、窒素導入管及び還
流コンデンサーを備えたフラスコに無水マレイン酸22
3gとイオン交換水320gを入れ、溶解させた。この
液に50%苛性ソーダ293gを滴下した後、液温を6
0゛Cとした。この液にタングステン酸ソーダ7.8g
を添加した後、30%過酸化水素水270gを添加した
。この際、フラスコを氷冷し、反応液の温度を60〜8
0°Cとなるように保った。その後、60°Cで1時間
保持し、エポキシコハク酸ソーダを得た。That is, maleic anhydride 22 was placed in a flask equipped with a thermometer, a stirrer, a dropping funnel, a nitrogen inlet tube, and a reflux condenser.
3 g and 320 g of ion-exchanged water were added and dissolved. After dropping 293g of 50% caustic soda into this liquid, the temperature of the liquid was lowered to 6.
It was set to 0°C. 7.8g of sodium tungstate in this liquid
After that, 270 g of 30% hydrogen peroxide solution was added. At this time, the flask was cooled with ice, and the temperature of the reaction solution was adjusted to 60-88℃.
The temperature was maintained at 0°C. Thereafter, the mixture was maintained at 60°C for 1 hour to obtain sodium epoxysuccinate.
次に、このエポキシコハク酸ソーダをPayneらの方
法に従って酸型とした後、過剰量のオルトギ酸エチルと
反応させることにより、エポキシコハク酸ジエチルエス
テルを得た。Next, this sodium epoxysuccinate was made into an acid form according to the method of Payne et al., and then reacted with an excess amount of ethyl orthoformate to obtain diethyl epoxysuccinate.
エポキシコハク酸ジエチルエステル21gを温度計、攪
拌機、窒素導入管及び脱水管付きフラスコに入れ、三弗
化ホウ素ジエチルエーテル錯体0.3gを添加した後、
100°C148時間保持した。得られた液をヘキサン
にて再沈澱を行い、乾燥後、苛性ソーダにてアルカリ加
水分解(80”C,24時間)を行うことによりポリエ
ポキシコハク酸ソーダを得た。After putting 21 g of epoxysuccinic acid diethyl ester into a flask equipped with a thermometer, a stirrer, a nitrogen introduction tube, and a dehydration tube, and adding 0.3 g of boron trifluoride diethyl ether complex,
The temperature was maintained at 100°C for 148 hours. The obtained liquid was reprecipitated with hexane, dried, and then alkaline hydrolyzed with caustic soda (80''C, 24 hours) to obtain sodium polyepoxysuccinate.
実施例1
本発明の水処理剤のスケール抑制剤としての効果を調べ
るため以下の試験を行った。Example 1 The following test was conducted to examine the effectiveness of the water treatment agent of the present invention as a scale inhibitor.
塩化カルシウム2水塩0.176%水溶液150gに、
表1に示す本発明化合物を有効分として1%含有する水
溶液を300μI添加し、更に炭酸水素ナトリウム0.
168%水溶液150gを加えた。pHを8.0に調整
した後、ガラスビンに入れ、密栓した後60℃に6時間
静置した0次いで冷却した後、沈澱物を0.1 μのメ
ンブレンフィルターで濾過し、濾液中のカルシウム濃度
をEDTA滴定により分析した。得られた結果を表1に
示した。To 150 g of calcium chloride dihydrate 0.176% aqueous solution,
300 μl of an aqueous solution containing 1% of the active ingredient of the compound of the present invention shown in Table 1 was added, and 0.0 μl of sodium bicarbonate was added.
150 g of a 168% aqueous solution was added. After adjusting the pH to 8.0, it was placed in a glass bottle, tightly stoppered, and left at 60°C for 6 hours. After cooling, the precipitate was filtered through a 0.1 μ membrane filter, and the calcium concentration in the filtrate was determined. was analyzed by EDTA titration. The results obtained are shown in Table 1.
また、比較のために、スケール抑制剤として、市販のポ
リマレイン酸、市販のポリアクリル酸ソーダおよび酒石
酸に対する結果も表1に示す。For comparison, Table 1 also shows the results for commercially available polymaleic acid, commercially available sodium polyacrylate, and tartaric acid as scale inhibitors.
表 1
注)
A :加熱前のCa濃度
B:試験後の濾液中のCa濃度
C:無添加での試験後の濾液中のCa1度実施例2
以下の水質を示す合成水11をビーカーにとり、これに
本発明の水処理剤及び比較試料を表2に示す所定量(固
型分として)加え、水温を50゛Cに保持した。この水
中に炭素鋼の試験片5S−41(45x20x 2 m
m)を浸漬し、その水をマグネチックスターラー、20
Orpmにより撹拌し、10日間その状態に保持した。Table 1 Note) A: Ca concentration before heating B: Ca concentration in the filtrate after the test C: 1 degree of Ca in the filtrate after the test without additives Example 2 Synthetic water 11 showing the following water quality was placed in a beaker, To this were added the water treatment agent of the present invention and a comparative sample in predetermined amounts (as solid content) shown in Table 2, and the water temperature was maintained at 50°C. Carbon steel specimen 5S-41 (45x20x2 m
m) and soak the water in a magnetic stirrer for 20 minutes.
It was stirred by Orpm and kept in that state for 10 days.
但し、その間試験水は2目間隔で交換した。However, during that time, the test water was replaced every two times.
試験後の腐食速度を表2に示す。Table 2 shows the corrosion rate after the test.
く合成水〉
p)+ 8.0
全 硬 度 200ppm (CaCOsとして
)カルシウム硬度 150ppm (CaCOsとし
て)門−アルカリ度 150ppm (CaCOiと
して)塩化物イオン 90ppm
硫酸イオン 60ppm
表 2
実施例3
海水加熱系に対するスケール抑制効果を調べるため以下
の試験を行った。Synthetic water p) + 8.0 Total hardness 200 ppm Calcium hardness 150 ppm (as CaCOs) Alkalinity 150 ppm (as CaCOi) Chloride ion 90 ppm Sulfate ion 60 ppm Table 2 Example 3 For seawater heating system The following tests were conducted to investigate the scale suppression effect.
内径6m糟のステンレスパイプ内を循環している海水を
、110℃に蒸気加熱できる試験機を用いて、濃縮倍率
2倍の人工海水を3201/Hrで20時間循環させた
。加熱器内のパイプに付着したスケールを、酸洗浄によ
り溶解後、原子吸光法により定量を行い、各スケール抑
制剤の抑制効果を調べた。Using a testing machine capable of steam heating seawater circulating in a stainless steel pipe with an inner diameter of 6 m to 110°C, artificial seawater with a concentration factor of 2 was circulated at 3201/Hr for 20 hours. The scale adhering to the pipes in the heater was dissolved by acid cleaning, and then quantified by atomic absorption spectroscopy to examine the inhibitory effects of each scale inhibitor.
結果を表3に示す。尚、表中の添加量は固型分としての
量である。The results are shown in Table 3. In addition, the amount added in the table is the amount as solid content.
表 3
注)
* :伝熱管単位面積当たりのCaCO5スケールとM
g (0)1) zスケールの総量を表す。Table 3 Note) *: CaCO5 scale and M per unit area of heat exchanger tube
g (0) 1) represents the total amount on the z scale.
Claims (1)
、一価若しくは二価の金属陽イオン、アンモニウムイオ
ン又は有機アミン陽イオンを表す。〕で示されるポリエ
ポキシコハク酸又はその塩からなることを特徴とする水
処理剤。[Claims] The following formula ▲ Numerical formulas, chemical formulas, tables, etc. ▼ (1) [In the formula, n represents an integer from 2 to 40, and X and Y are hydrogen atoms, monovalent or divalent metal atoms, ion, ammonium ion or organic amine cation. ] A water treatment agent comprising polyepoxysuccinic acid or a salt thereof.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29315690A JPH04166298A (en) | 1990-10-30 | 1990-10-30 | Water treating agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29315690A JPH04166298A (en) | 1990-10-30 | 1990-10-30 | Water treating agent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04166298A true JPH04166298A (en) | 1992-06-12 |
Family
ID=17791146
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29315690A Pending JPH04166298A (en) | 1990-10-30 | 1990-10-30 | Water treating agent |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04166298A (en) |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0599485A1 (en) * | 1992-11-19 | 1994-06-01 | Betz Europe, Inc. | Method of inhibiting corrosion in aqueous systems |
| EP0609590A1 (en) * | 1993-01-06 | 1994-08-10 | W.R. Grace & Co.-Conn. | Method for inhibiting corrosion of metals using polytartaric acids |
| EP0628539A1 (en) * | 1993-06-09 | 1994-12-14 | Betz Europe, Inc. | Polyepoxysuccinic acid derivatives and their use for the control of scale formation and corrosion in aqueous systems |
| US5489666A (en) * | 1993-06-09 | 1996-02-06 | Betz Laboratories, Inc. | Control of scale formation in aqueous systems |
| US5562830A (en) * | 1995-09-14 | 1996-10-08 | Betz Laboratories, Inc. | Calcium carbonate scale controlling method |
| US5616278A (en) * | 1993-08-13 | 1997-04-01 | Betzdearborn Inc. | Inhibition of scale and corrosion in aqueous systems |
| US8361952B2 (en) | 2010-07-28 | 2013-01-29 | Ecolab Usa Inc. | Stability enhancement agent for solid detergent compositions |
| WO2014119788A1 (en) * | 2013-02-04 | 2014-08-07 | 栗田工業株式会社 | Method for inhibiting corrosion in closed-circulation-type cooling water system |
| CN105461085A (en) * | 2016-01-07 | 2016-04-06 | 万全军 | Non-phosphorus environmentally-friendly corrosion-inhibition scale-inhibition dispersion agent and preparation method and application thereof |
| WO2019230757A1 (en) * | 2018-05-30 | 2019-12-05 | 栗田工業株式会社 | Initial treatment agent for circulating cooling water and method for preventing corrosion in circulating cooling water system |
| JP2019210545A (en) * | 2018-05-30 | 2019-12-12 | 栗田工業株式会社 | Initial treatment agent for circulating cooling water and method for preventing corrosion of circulating cooling water system |
| EP3631047A1 (en) * | 2017-05-24 | 2020-04-08 | BL Technologies, Inc. | Polyacrylate polymers for low carbon steel corrosion control |
| WO2020090526A1 (en) * | 2018-11-01 | 2020-05-07 | 栗田工業株式会社 | Method for inhibiting corrosion of metal member of cooling water system |
| CN115667585A (en) * | 2020-05-28 | 2023-01-31 | 埃科莱布美国股份有限公司 | Closed-loop cooling water corrosion inhibition using polymaleate and non-borate buffers |
| US12546014B2 (en) | 2021-05-05 | 2026-02-10 | Ecolab Usa Inc. | Closed loop cooling water corrosion inhibition employing polymaleates and non-borate buffers |
-
1990
- 1990-10-30 JP JP29315690A patent/JPH04166298A/en active Pending
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0599485A1 (en) * | 1992-11-19 | 1994-06-01 | Betz Europe, Inc. | Method of inhibiting corrosion in aqueous systems |
| EP0609590A1 (en) * | 1993-01-06 | 1994-08-10 | W.R. Grace & Co.-Conn. | Method for inhibiting corrosion of metals using polytartaric acids |
| US5344590A (en) * | 1993-01-06 | 1994-09-06 | W. R. Grace & Co.-Conn. | Method for inhibiting corrosion of metals using polytartaric acids |
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