WO2005116296A1 - 冷却水の処理方法及び処理薬剤 - Google Patents

冷却水の処理方法及び処理薬剤 Download PDF

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Publication number
WO2005116296A1
WO2005116296A1 PCT/JP2005/001472 JP2005001472W WO2005116296A1 WO 2005116296 A1 WO2005116296 A1 WO 2005116296A1 JP 2005001472 W JP2005001472 W JP 2005001472W WO 2005116296 A1 WO2005116296 A1 WO 2005116296A1
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WIPO (PCT)
Prior art keywords
acid
calcium carbonate
cooling water
group
calcium
Prior art date
Application number
PCT/JP2005/001472
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English (en)
French (fr)
Japanese (ja)
Inventor
Hideo Otaka
Masayori Koda
Hajime Iseri
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 JP2006513807A priority Critical patent/JP4725513B2/ja
Publication of WO2005116296A1 publication Critical patent/WO2005116296A1/ja

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • C02F5/14Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing phosphorus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • 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
    • C23F11/12Oxygen-containing compounds
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F11/00Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
    • C23F11/08Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
    • C23F11/10Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids using organic inhibitors
    • C23F11/173Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply
    • C02F2103/023Water in cooling circuits
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/08Corrosion inhibition

Definitions

  • the present invention relates to a treatment method and a treatment agent for simultaneously preventing corrosion of metal and scale failure in an open circulation cooling water system.
  • Metal members provided in the open circulating cooling water system for example, heat exchangers, reactors, and pipes made of carbon steel, copper, or copper alloy are corroded by contact with cooling water.
  • anticorrosion treatment is performed by adding a chemical.
  • Carbon steel heat exchangers In order to suppress corrosion of the reaction vessel and piping, phosphorus oxides such as orthophosphate, hexametaphosphate, hydroxyethylidene diphosphonate, and phosphonobutanetricarboxylate are used. The compound has been added to the cooling water. In some cases, heavy metal salts such as zinc salts and dichromates are added alone or in combination. The use of large amounts of these phosphorus compounds and heavy metal salts, especially heavy metal salts, can pollute water quality and seriously affect the environment, requiring great care and expense in handling and wastewater treatment. Become.
  • Nitrogen-containing azoles and phosphorus-zinc-based chemicals are mainly used for corrosion prevention of copper and copper alloy materials. If cooling water containing a large amount of nitrogen-containing chemicals or phosphorus is discharged into a closed water area, their concentration in the water area increases, and eutrophication tends to cause red tide and the like.
  • Phosphoric acid or polymerized phosphoric acid or other maleic acid or maleic acid polymer is effective for preventing precipitation of calcium carbonate.
  • these compounds are added to the open circulation cooling water system to prevent precipitation of calcium carbonate and prevent scale disturbance (for example, Japanese Patent Application Laid-Open No. 9-174092).
  • scale disturbance for example, Japanese Patent Application Laid-Open No. 9-174092.
  • the water quality of the aqueous system exceeds the limit of calcium carbonate precipitation prevention performance of these compounds, crystallization of calcium carbonate proceeds rapidly, leading to scale disturbance.
  • the same obstacle is caused by the precipitation of calcium phosphate and calcium phosphate zinc. Therefore, the applicable water quality of these compounds is limited, and the upper limit of the concentration multiple is also limited.
  • the present invention provides a method and a chemical for treating cooling water that simultaneously prevent corrosion and scale failure of equipment, piping, and equipment made of metal such as carbonated steel, copper, and copper alloy in an open-circulating cooling water system.
  • the purpose is to:
  • the method for treating cooling water of the present invention is a method for treating cooling water that suppresses corrosion of metals in the cooling water system and prevents scale failure, wherein the cooling water contains a calcium carbonate precipitation inhibitor and a carbonate. A calcium dispersant is added, and calcium carbonate fine particles are dispersed in the cooling water to form an anticorrosion film on the metal surface.
  • the agent for treating cooling water of the present invention is one or two selected from the group consisting of a phosphonic acid compound represented by the following I, a carboxylic acid polymer represented by the following II, and a carboxylic acid copolymer represented by the following III: 5 to 95% by weight of the above calcium carbonate precipitation inhibitor, and at least one calcium carbonate dispersant 5 selected from the group consisting of a carboxylic acid copolymer of the following IV and a nonionic polymer of the following V — Contains 95% by weight.
  • polyacrylic acid polymethacrylic acid, polymaleic acid, polyitaconic acid, polyacrylate, At least one of polymethacrylate, polymaleate, and polyitaconate.
  • One or more carboxylic acid components selected from the group consisting of acrylic acid, methacrylic acid, maleic acid, itaconic acid and salts thereof, at least 40 mol%, and alkane, styrene and styrene having 4 to 10 carbon atoms.
  • a copolymer containing at least one unsaturated hydrocarbon component selected from the group consisting of dicyclopentadiene and 5 mol% or more.
  • carboxylic acid components selected from the group consisting of acrylic acid, methacrylic acid, maleic acid, itaconic acid, and salts thereof, and butylsulfonic acid, arylsulfonic acid, and styrenesulfonic acid.
  • V At least one of polyacrylamide, polybutyl alcohol, polyethylene glycol, polypropylene glycol, and ethylene glycol propylene glycol block copolymer.
  • FIG. 1 is a system diagram showing an outline of a bench scale cooling water system evaluation test apparatus used in Examples and Comparative Examples.
  • the fine calcium carbonate fine particles dispersed in water prevent excessive scale adhesion and prevent scale damage.
  • a carbonated calcium precipitation inhibitor and a calcium carbonate dispersant are added to cooling water.
  • the calcium carbonate precipitation inhibitor suppresses the precipitation of calcium carbonate.
  • the calcium carbonate dispersant prevents the calcium carbonate generated in the water of quality exceeding the performance limit of the calcium carbonate precipitation inhibitor from becoming coarse.
  • the metal in the cooling water system A stable anti-corrosion film of calcium carbonate with an adequate thickness that exhibits a sufficient anti-corrosion effect can be quickly and stably formed on the surface of the steel to suppress the corrosion of the metal and reliably prevent scale damage. can do.
  • the calcium carbonate precipitation inhibitor added to the cooling water those which can be used, for example, those conventionally used as a scale inhibitor for calcium carbonate are preferably used.
  • a carboxylic acid polymer II and a carboxylic acid copolymer III are preferably used.
  • I at least one of hydroxyethylidene diphosphonic acid, 2-phosphonobutane 1,2,4 tricarboxylic acid, aminotrimethylene phosphonic acid, 1 phosphonobutane 1,2,3,4-tetracarboxylic acid, and phosphonofumaric acid.
  • At least one of polyacrylic acid, polymethacrylic acid, polymaleic acid, polyitaconic acid, polyacrylate, polymethacrylate, polymaleate, and polyitaconate At least one of polyacrylic acid, polymethacrylic acid, polymaleic acid, polyitaconic acid, polyacrylate, polymethacrylate, polymaleate, and polyitaconate.
  • the molecular weight of these carboxylic acid polymers is about 500-5000.
  • carboxylic acid components selected from the group consisting of acrylic acid, methacrylic acid, maleic acid, itaconic acid and salts thereof, at least 40 mol%, preferably 50-90 mol%, and 4 carbon atoms.
  • unsaturated hydrocarbon components such as 10 alkenes (eg, isobutylene, butylene, pentene, etc.), styrene, and dicyclopentadiene one or more selected at least 5 mol% or more, preferably 10-50 mol%;
  • a copolymer comprising: The molecular weight of these carboxylic acid-based copolymers is preferably about 1,000 to 20,000.
  • the calcium carbonate dispersant preferably, when calcium carbonate is adsorbed by a carboxyl group, a charged hydrophilic group such as a sulfone group or a hydrophobic group such as an ether is oriented to the outside so that particles can approach each other.
  • a compound having a functional group that prevents the above is used, and examples thereof include one or more members selected from the group consisting of a carboxylic acid-based copolymer of the following IV and a nonionic polymer of the following V.
  • the molecular weight of these carboxylic acid-based copolymers is preferably about 1000-20000.
  • V At least one of polyacrylamide, polybutyl alcohol, polyethylene glycol, polypropylene glycol, and ethylene glycol propylene glycol block copolymer.
  • the molecular weight of these nonionic polymers is preferably about 5,000 to 100,000.
  • the amounts of the calcium carbonate precipitation inhibitor and the calcium carbonate dispersant added to the cooling water are generally each 100 mg ZL, preferably 5 to 50 mg ZL, respectively. It is about 10-100 mgZL in total with the dispersant. If the amounts of the calcium carbonate precipitation inhibitor and the calcium carbonate dispersant are too small, sufficient effects cannot be obtained, while if too large, it is uneconomical and the generation of calcium carbonate fine particles may be delayed. Furthermore, in particular, in the case of a phosphorus conjugate, a problem of precipitation of calcium phosphate and a problem of wastewater treatment occur, which is not preferable.
  • the required amount of calcium carbonate fine particles to be dispersed in the cooling water is generally about 110 OOmgZL, preferably about 5-100mgZL. If the amount of carbonic acid ruthenium particles dispersed in the cooling water is too small, a sufficient anticorrosion effect cannot be obtained, and if it is too large, scale failure may occur.
  • the particle size of the calcium carbonate fine particles dispersed in the cooling water is larger than 10 m or smaller than 0.01 ⁇ m, the particle size does not significantly contribute to the formation of the anticorrosive film. It is preferable that 0.01 to 10 / zm of calcium carbonate fine particles be contained in water in an amount of 1 lOOOOmgZL, particularly 5lOOmgZL. However, calcium carbonate having a particle size of less than 0.01 ⁇ m or more than 10 m may be contained in the water. Such calcium carbonate fine particles can be produced by using a calcium carbonate precipitation inhibitor and a calcium carbonate dispersant in combination.
  • the cooling water is calculated according to the water temperature. Make the hardness, M alkalinity, pH, etc. above a certain value.
  • the supersaturation degree of the cooling water is preferably set to about 1.2 to 3.5 as a saturation index (saturation index (SI) or a Langelier index).
  • calcium carbonate coarse particles were prepared by crushing calcium carbonate coarse particles using a fine crusher such as a tornado mill.
  • the calcium carbonate fine particles may be added to the cooling water, but preferably a method of chemically depositing calcium carbonate fine particles in the cooling water as described below is advantageous.
  • One or more calcium salts such as calcium chloride, calcium nitrate, calcium hydroxide, etc., and bicarbonates such as sodium bicarbonate, potassium bicarbonate, lithium bicarbonate, sodium carbonate, potassium carbonate , A carbonate such as lithium carbonate, and one or more alkali metal hydroxides such as sodium hydroxide, potassium hydroxide, and lithium hydroxide, and contact with air in a cooling tower.
  • a GO heat exchanger raise the temperature of the cooling water, reduce the solubility of calcium carbonate, and precipitate and disperse the calcium carbonate fine particles.
  • agents used in ordinary water treatment other than the calcium carbonate precipitation inhibitor and the calcium carbonate dispersant may be added in combination as needed.
  • an aqueous system contains a copper material
  • an azole derivative such as benzotriazole or tolyltriazole
  • a bactericide such as sodium hypochlorite may be added in combination.
  • the treatment agent for cooling water of the present invention contains the above-mentioned calcium carbonate precipitation inhibitor and calcium carbonate dispersant according to the present invention.
  • the calcium carbonate precipitation inhibitor and the calcium carbonate dispersant are each usually contained in an amount of 5 to 95% by weight, preferably 20 to 80% by weight.
  • the treatment agent of the present invention is one in which the calcium carbonate precipitation inhibitor and the calcium carbonate dispersant are separately supplied even if the calcium carbonate precipitation inhibitor and the calcium carbonate dispersant are mixed in advance. May be. Further, it may contain various agents other than the carbonated calcium precipitation inhibitor and the calcium carbonate dispersant.
  • Example 117 Comparative Example 114
  • a Maleic acid / noacrylic acid Z styrene copolymer (molar ratio: 60:25:15, molecular weight: 10,000)
  • Acrylic acid Z vinyl sulfonic acid copolymer (molar ratio 75:25, molecular weight 5,000) d Acrylic acid noallyl sulfonic acid copolymer (molar ratio 70.30, molecular weight 3,000) e Acrylic acid Styrene sulfonic acid copolymer Combined (molar ratio: 80:20, molecular weight: 8,000) Acrylic acid / 3-aryloxy-1-hydroxypropanesulfonic acid copolymer
  • Acrylic acid / hydroxy methacrylate isoprene sulfonic acid copolymer g (molar ratio 70:10:20, molecular weight 13,000)
  • circulating cooling water is sent from cooling tower 1 to heat exchanger 3 by circulation pipe 2 having pump ⁇ ⁇ , and return water is returned to cooling tower 1 from pipe 4.
  • . 5 is a supply water supply pipe
  • 6 is a sodium hypochlorite aqueous solution supply pipe
  • 7 is a chemical supply pipe shown in Table 3
  • 8 is a blow pipe, each equipped with pumps ⁇ ⁇ ⁇ , ⁇ , ⁇ , ⁇ .
  • Reference numeral 9 denotes a bypass pipe having a valve 9a.
  • Heat exchanger inlet water temperature 30 ° C
  • Heat exchanger outlet water temperature 50 ° C (steam heating)
  • Drug addition amount The drugs shown in Table 4 were added at the addition concentrations shown in Table 4.
  • the above operation was performed for 30 days, and the Z-day corrosion rate (carbon steel) was measured once using a corrosion meter.
  • the analysis of the calcium hardness of the cooling water was performed once every Z weeks, the cooling water was filtered with a 0.1 m millipore filter, and the calcium hardness of the filtrate was determined by titration.
  • the calcium hardness of the filter was measured by atomic absorption spectrometry after boiling with hydrochloric acid.
  • test tube was taken out of the heat exchanger, dried, cut every 20 cm, and subjected to evaluation of deposits and pitting corrosion.
  • the deposit on the test tube was taken using a metal brush, and the scale deposition rate was calculated from the dry weight and the tube area.
  • test tubes from which the deposits had been collected were pickled with hydrochloric acid containing an inhibitor to remove corrosion products.
  • the pit depth on the test tube surface was measured using a depth gauge, and the maximum value was determined.
  • Table 4 shows the calcium hardness of the filtrate, the calcium hardness of the amount captured by filtration, the corrosion rate and pit depth of the tubes of the heat exchanger, and the scale adhesion rate. The average values during the period were used for the measured values of the corrosion rate, the calcium hardness of the filtrate, and the calcium hardness of the amount captured by filtration.
  • Table 4 shows the value obtained by multiplying the calcium hardness of the makeup water (industrial water) by the concentration ratio, and The sum of the calcium hardness of the sample and the calcium hardness of the amount captured by filtration was subtracted, and the resulting value was also recorded as an index of the tendency to scale.
  • the saturation index of the calcium carbonate dissolved in the cooling water at this time is as shown in Table 4, and the calcium carbonate fine particles having a particle size of 0.01-10 / zm dispersed in the cooling water are shown in Table 4.
  • the amount was from 0 to 30 mg ZL from the value of the calcium hardness of the 0.1 ⁇ m filtration trap.
  • the filter trap is a gel of polymer and calcium ions.
  • the main component of the deposit is calcium phosphate
  • the main component of the deposit is magnesium silicate

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
PCT/JP2005/001472 2004-05-25 2005-02-02 冷却水の処理方法及び処理薬剤 WO2005116296A1 (ja)

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CN (1) CN100395199C (enrdf_load_stackoverflow)
MY (1) MY146543A (enrdf_load_stackoverflow)
TW (1) TW200538405A (enrdf_load_stackoverflow)
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JP2008249285A (ja) * 2007-03-30 2008-10-16 Hakuto Co Ltd 開放循環式冷却水系の水処理方法及び開放循環式冷却水系用水処理剤
JP2011045861A (ja) * 2009-08-28 2011-03-10 Hakuto Co Ltd 水処理剤および水処理方法
CN101565660B (zh) * 2009-06-02 2011-08-17 董宇新 一种有机除垢组合物及其制备方法和应用
CN102414798A (zh) * 2009-04-27 2012-04-11 韩商Snu精密股份有限公司 原料供应单元、薄膜沉积装置及沉积薄膜的方法
JP2013188729A (ja) * 2012-03-15 2013-09-26 Kurita Water Ind Ltd 蒸気発生器の鉄スケール防止剤及び防止方法
WO2015122264A1 (ja) * 2014-02-13 2015-08-20 栗田工業株式会社 蒸気発生設備のスケール除去方法及びスケール除去剤
CN105347557A (zh) * 2015-11-19 2016-02-24 四川省宜宾惠美线业有限责任公司 一种制冷机组在枯水期的冷却水处理系统
JP2017170348A (ja) * 2016-03-24 2017-09-28 栗田工業株式会社 逆浸透膜用スケール防止剤及び逆浸透膜処理方法
JP2023066238A (ja) * 2021-10-28 2023-05-15 伯東株式会社 初期処理方法
JP7601147B1 (ja) 2023-07-10 2024-12-17 栗田工業株式会社 密閉冷却水系のpH制御方法及び装置

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CN104310598A (zh) * 2014-10-22 2015-01-28 山东华亚环保科技有限公司 一种用于浓缩海水装置的缓蚀剂
CN104310606A (zh) * 2014-10-22 2015-01-28 山东华亚环保科技有限公司 一种用于浓缩海水装置的缓蚀剂
CN104525897A (zh) * 2015-01-08 2015-04-22 浙江万丰奥威汽轮股份有限公司 一种低压铸造模具的新型冷却介质
JP6128171B2 (ja) 2015-07-09 2017-05-17 栗田工業株式会社 冷却排出水の回収方法及び回収装置
CN105481116B (zh) * 2015-12-18 2018-07-20 广东顺德朗新环保有限公司 一种循环冷却水缓蚀阻垢剂及其制备方法
AU2018271842B2 (en) * 2017-05-24 2023-07-27 Bl Technologies, Inc. Polyacrylate polymers for low carbon steel corrosion control
CN113800653A (zh) * 2020-06-16 2021-12-17 中国石油化工集团有限公司 一种地热流体阻垢剂及其制备方法和应用
CN114106788B (zh) * 2021-12-15 2024-07-26 湖南省希润弗高分子新材料有限公司 一种工业循环冷却液

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Cited By (18)

* Cited by examiner, † Cited by third party
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JP2008249285A (ja) * 2007-03-30 2008-10-16 Hakuto Co Ltd 開放循環式冷却水系の水処理方法及び開放循環式冷却水系用水処理剤
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