WO2008006855A2 - Inhibition of corrosion in cooling water system - Google Patents
Inhibition of corrosion in cooling water system Download PDFInfo
- Publication number
- WO2008006855A2 WO2008006855A2 PCT/EP2007/057115 EP2007057115W WO2008006855A2 WO 2008006855 A2 WO2008006855 A2 WO 2008006855A2 EP 2007057115 W EP2007057115 W EP 2007057115W WO 2008006855 A2 WO2008006855 A2 WO 2008006855A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- cooling water
- corrosion
- water system
- alkylalkanolamine
- copper
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-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
- C23F14/00—Inhibiting incrustation in apparatus for heating liquids for physical or chemical purposes
- C23F14/02—Inhibiting incrustation in apparatus for heating liquids for physical or chemical purposes by chemical means
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
- C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
- C02F5/12—Treatment 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 nitrogen
- C02F5/125—Treatment 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 nitrogen combined with inorganic substances
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-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
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting 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
- C23F11/14—Nitrogen-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C23—COATING 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
- C23F—NON-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
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
- C23F11/10—Inhibiting 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
- C23F11/14—Nitrogen-containing compounds
- C23F11/141—Amines; Quaternary ammonium compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
- C02F1/683—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water by addition of complex-forming compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/023—Water in cooling circuits
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/08—Corrosion inhibition
Definitions
- This present invention relates to novel methods of controlling corrosion in cooling water systems, and more particularly to certain alkylalkanolamincs which have been found to be effective for controlling corrosion of ferrous-based and copper-based metals which are in contact with cooling water systems.
- Iron and iron-based metal alloys containing alloys such as mild steel are well- known materials used in constructing the apparatus of cooling water systems. Copper and copper-base metals also find significant use in cooling water systems. In these systems cooling water circulates, contacts the iron and/or copper based metal surfaces, and may be concentrated, such as by evaporation of a portion of the water from the system. Even though iron and copper based metals arc readily subject to corrosion in aqueous environments, they are used over other metals due to their strength and availability.
- iron-based metals shall mean any iron metal and/or metal alloys containing iron therein.
- copper based metal shall mean any copper metal and/or metal alloys containing copper therein.
- Typical systems in which the iron and/or copper metal parts are subject to corrosion include evaporators, single and multi-pass heat exchangers, cooling towers, and associated equipment and the like. As the cooling water passes through or over the system, a portion of the system water evaporates thereby increasing the concentration of the dissolved materials contained in the system. These materials approach and reach a concentration at which they may cause severe pitting and corrosion which eventually requires replacement of the metal parts.
- Various corrosion inhibitors have been previously used to treat these systems.
- chromates, inorganic phosphates and/or polyphosphates have been used to inhibit the corrosion of metals which are in contact with water.
- the chromates though effective, are highly toxic and consequently present handling and disposal problems.
- phosphates are non-toxic, due to the limited solubility of calcium phosphate, it is difficult to maintain adequate concentrations of phosphates in many cooling water systems.
- Polyphosphates are also relatively non-toxic, but tend to hydrolyzc to form orthophosphate which in turn, like phosphate itself, can create scale and sludge problems in cooling water systems (e.g. by combining with calcium in the system to form calcium phosphate).
- excess phosphate compounds can serve as nutrient sources. Borates, nitrates, and nitrites have also been used for corrosion inhibition. These too can serve as nutrients in low concentrations, and/or represent potential health concerns at high concentrations.
- This invention is directed to certain alkylalkanolamine compounds and to their use as corrosion control agents for treating cooling water systems.
- the method of this invention comprises adding to a cooling water system, in an amount effective to inhibit corrosion of ferrous-based and/or copper-based metals which are in contact with the cooling water system alkylalkanolamine compounds having the following general formula:
- the precise dosage of the corrosion inhibiting agents of this invention depends, to some extent, on the nature of the cooling water system in which it is to be incorporated and the degree of protection desired.
- the concentration of alkylalkanolamine compounds maintained in the system preferably range from about 1.000 ppm to about 6,000 ppm. Within this range, generally lower dosages of about 2,000 ppm or less are more preferred, with a dosage of about 1 ,500 ppm or less being most preferred for many cooling water systems, such as for example, many closed recirculating cooling water systems.
- the exact amount required with respect to a particular aqueous system can be readily determined by one of ordinary skill in the art in conventional manner.
- the corrosion inhibiting agents of the present invention are best suited for recirculating cooling water systems, open or closed, because of the preferred treatment dosages. However, use in once through systems would recognize the corrosion protection provided by the present invention.
- the pH is preferably maintained at 7 or above, and is most preferably maintained at 8 or above.
- the alkylalkanolamine compounds of the present invention also provide for pH control/adjustment of the cooling water system.
- the corrosion inhibiting compositions of this invention may be added to the system water by any convenient mode, such as by first forming a concentrated solution of the treating agent with water, preferably containing between 1 and 50 total weight percent of the alkylalkanolamine compounds.
- treatment compositions may be added to the make-up water or feed water lines through which water enters the system.
- an injection calibrated to deliver a predetermined amount periodically or continuously to the make-up water may be employed.
- the present invention is particularly useful in the treatment of cooling water systems which operate at temperatures between 60 0 F and 200 0 F, particularly recirculating cooling water systems which operate at temperatures of from about 80 0 F to 150 0 F.
- chemical corrosion inhibiting compositions of the present invention may be used as the sole corrosion inhibitor for the cooling water system
- other conventional water treatment compositions customarily employed in cooling water systems may advantageously be used in combination with the claimed treatment agents.
- other water treatment additives which may be used include, but are not limited to, biocides, scale inhibitors, chelants, sequestering agents, dispersing agents, other corrosion inhibitors, polymeric agents, oxygen scavengers and the like.
- DGA diglycolamine, 2-(2-hydroxyethoxy)ethylamine
- IPAE isopropylaminoethanol
- the HIvB of an alkanolamine can be calculated with the following formula:
- HLB 20[ ⁇ 60 (for monoethoxylate) or 104 (for diethoxylate)) ⁇ GMW]
- alkanolamines having lower HLB values provide enhanced corrosion control of ferrous-based and/or copper-based metals in cooling water systems.
- Alkanolamines having HLB values of 7 - 12 are preferred.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Abstract
Λ method of controlling corrosion in cooling water systems is disclosed which includes introducing into the cooling water system certain alkylalkanolamine compounds having the general formula: Rx-NHz-(CH2CH2OH)y wherein R is a C3 to C8 alkyl group either linear or branched, x and y are 1 or 2, z is 0 or I, x+y is not greater than 3, z = 3-x-y and the R groups are either the same or different C3 to C8 alkyl groups.
Description
Inhibition of corrosion in cooling water system.
FIELD OF THE INVENTION
This present invention relates to novel methods of controlling corrosion in cooling water systems, and more particularly to certain alkylalkanolamincs which have been found to be effective for controlling corrosion of ferrous-based and copper-based metals which are in contact with cooling water systems.
BACKGROUND OF THE INVENTION
Iron and iron-based metal alloys containing alloys such as mild steel are well- known materials used in constructing the apparatus of cooling water systems. Copper and copper-base metals also find significant use in cooling water systems. In these systems cooling water circulates, contacts the iron and/or copper based metal surfaces, and may be concentrated, such as by evaporation of a portion of the water from the system. Even though iron and copper based metals arc readily subject to corrosion in aqueous environments, they are used over other metals due to their strength and availability.
It is known that various materials which are naturally or synthetically occurring in the cooling water systems, especially systems using water derived from natural resources such as seawater, rivers, lakes and the like, attack such metals. The term "ferrous-based metals", as used herein, shall mean any iron metal and/or metal alloys containing iron therein. The term "copper based metal", as used herein, shall mean any copper metal and/or metal alloys containing copper therein. Typical systems in which the iron and/or copper metal parts are subject to corrosion include evaporators, single and multi-pass heat exchangers, cooling towers, and associated equipment and the like. As the cooling water passes through or over the system, a portion of the system water evaporates thereby increasing the concentration of the dissolved materials contained in the system. These materials approach and reach a concentration at which they may cause severe pitting and corrosion which eventually requires replacement of the metal parts. Various corrosion inhibitors have been previously used to treat these
systems.
For example, chromates, inorganic phosphates and/or polyphosphates have been used to inhibit the corrosion of metals which are in contact with water. The chromates, though effective, are highly toxic and consequently present handling and disposal problems. While phosphates are non-toxic, due to the limited solubility of calcium phosphate, it is difficult to maintain adequate concentrations of phosphates in many cooling water systems. Polyphosphates are also relatively non-toxic, but tend to hydrolyzc to form orthophosphate which in turn, like phosphate itself, can create scale and sludge problems in cooling water systems (e.g. by combining with calcium in the system to form calcium phosphate). Moreover, where there is concern over eutrophication of receiving waters, excess phosphate compounds can serve as nutrient sources. Borates, nitrates, and nitrites have also been used for corrosion inhibition. These too can serve as nutrients in low concentrations, and/or represent potential health concerns at high concentrations.
Environmental considerations have also recently increased concerns over the discharge of other corrosion inhibiting metals such as zinc, which previously were considered acceptable for water treatment.
SUMMARY OF THE INVENTION
It is an object of this invention to provide a method of inhibiting the corrosion of ferrous and/or copper based metals in contact with a cooling water system.
It is another object of this invention to provide a method of inhibiting corrosion of ferrous and/or copper based metals in contact with a cooling water system with surprisingly enhanced results.
In accordance, with the present invention, there has been provided a method for inhibiting corrosion of ferrous and/or copper based metals which are in contact with a cooling water system comprising adding to the system a corrosion inhibiting amount of an alkylalkanolamine.
DESCRIPTION OF THE INVENTION
This invention is directed to certain alkylalkanolamine compounds and to their use as corrosion control agents for treating cooling water systems. The method of this invention comprises adding to a cooling water system, in an amount effective to inhibit corrosion of ferrous-based and/or copper-based metals which are in contact with the cooling water system alkylalkanolamine compounds having the following general formula:
Rx-NH,-(CH2CH2OH)y
wherein R is a C3 to Q alkyl group either linear or branched, x and y are 1 or 2, z is 0 or 1 , x+y is not greater than 3, z = 3-x-y and the R groups are either the same or different C-, to Cg alkyl groups.
The precise dosage of the corrosion inhibiting agents of this invention depends, to some extent, on the nature of the cooling water system in which it is to be incorporated and the degree of protection desired. In general, however, the concentration of alkylalkanolamine compounds maintained in the system preferably range from about 1.000 ppm to about 6,000 ppm. Within this range, generally lower dosages of about 2,000 ppm or less are more preferred, with a dosage of about 1 ,500 ppm or less being most preferred for many cooling water systems, such as for example, many closed recirculating cooling water systems. The exact amount required with respect to a particular aqueous system can be readily determined by one of ordinary skill in the art in conventional manner. The corrosion inhibiting agents of the present invention are best suited for recirculating cooling water systems, open or closed, because of the preferred treatment dosages. However, use in once through systems would recognize the corrosion protection provided by the present invention. As is typical of most cooling water systems, the pH is preferably maintained at 7 or above, and is most preferably maintained at 8 or above. In addition to providing for corrosion control, the alkylalkanolamine compounds of the present invention also provide for pH control/adjustment of the cooling water system.
The corrosion inhibiting compositions of this invention may be added to the system water by any convenient mode, such as by first forming a concentrated solution of the treating agent with water, preferably containing between 1 and 50 total weight percent of the alkylalkanolamine compounds.
This concentrate is then feed to the cooling water system at some convenient point in the system. In many instances, the treatment compositions may be added to the make-up water or feed water lines through which water enters the system.
For example, an injection calibrated to deliver a predetermined amount periodically or continuously to the make-up water may be employed.
The present invention is particularly useful in the treatment of cooling water systems which operate at temperatures between 60 0F and 200 0F, particularly recirculating cooling water systems which operate at temperatures of from about 80 0F to 150 0F.
It will be appreciated that while the chemical corrosion inhibiting compositions of the present invention may be used as the sole corrosion inhibitor for the cooling water system, other conventional water treatment compositions customarily employed in cooling water systems may advantageously be used in combination with the claimed treatment agents. Thus, other water treatment additives which may be used include, but are not limited to, biocides, scale inhibitors, chelants, sequestering agents, dispersing agents, other corrosion inhibitors, polymeric agents, oxygen scavengers and the like.
EXAMPLES
Glossary:
BΛE: 2-butylaminoethanol
BDEA: butyldiethanolamine
AMP-95: 2-amino-2-methyl-l -propanol
DGA: diglycolamine, 2-(2-hydroxyethoxy)ethylamine
MEA: monoethanolamine
TEA: triethanolamine
DIPAE: diisopropylaminoethanol
IPAE: isopropylaminoethanol
Example 1 :
Brass (2"' x 2" x 0.032") panels were immersed into aqueous solutions of alkanolamine (0.3 M) and octanoic acid (0.2 M) adjusted with IΪ3PO4 and/or KOH to pH = 8.5 at room temperature. A 450 gram portion of each solution was weighed carefully and transferred to a wide-mouth screw-cap glass bottle. The brass panels were washed with 10% liquid-Nox (Alcanox product) and buffed dry with a paper towel. The panels were immersed in the solutions (all panels
oriented at the same angle within the solution) and the cap placed tightly on the jar. Λ 5 gram sample of each solution was collected at regular intervals and analyzed by ICP/cmission for metals content. In the case of brass, both a leaded (CΛ-360, 3% Pb) and an unleaded (CΛ-260) alloy were employed. The results for leaching of copper, zinc and lead after 30 days of immersion are shown below.
Table :
Cu, Pb, and Zn Results - Day 30, Octanoic Λcid, Unleaded Brass:
The data in Table I clearly show that the alkylalkanolamine compounds of the present invention (BAE, BDFiA, DIPAE and IPAE) provided inhibition of corrosion of the copper alloys.
Table Il
Cu, Pb, and Zn Results - Day 30, Octanoic Acid, Leaded Brass:
The data in Table II clearly shows that the alkylalkanolamine compounds of the present invention (BAE, BDEA, DIPAE and IPAE) provide improved inhibition of corrosion of copper alloys.
Example 2:
The corrosion of carbon steel in 0.3M solutions of octanoic acid neutralized with 0.2M alkanolamine followed by pH adjustment with KOH/H3PO4 to pH = 8.5 was assessed with polarization resistance experiments. The data, converted to a corrosion rate in mils per year, is set forth in Table III. The data in Table III shows the low corrosion rate provided by the alkylalkanolamine, BAE, in accordance with the present invention.
Table III
Alkanolamine Corrosion Rate (mils/year)
BAE 0.4
AMP 0.25
DGA ».90
MEA 7.03
Example
The HIvB of an alkanolamine can be calculated with the following formula:
HLB = 20[{60 (for monoethoxylate) or 104 (for diethoxylate)) ÷ GMW]
A "fable of HLB values calculated by this formula is given below:
1 able IV
The data in Table IV, in combination with data in Tables I, II and III shows that alkanolamines having lower HLB values provide enhanced corrosion control of ferrous-based and/or copper-based metals in cooling water systems. Alkanolamines having HLB values of 7 - 12 are preferred.
Having described the invention, we now claim the following and their equivalents.
Claims
1 . Λ method for inhibiting corrosion of ferrous and/or copper metals in contact with a cooling water system comprising adding to the system an alkylalkanolamine of the general formula
RX-NI MCH2CH2OHX
wherein R is a C3-C8 linear or branched alkyl group, x and y are 1 or 2, z is 0 or 1 , x+y if less than or equal to 3, and z=3-x-y.
2. The method of claim 1 wherein said alkylalkanolamine is selected from the group consisting of 2-butylaminoethanol, butyldiethanolamine, diisopropylaminocthanol and isopropylaminoethanol.
3. The method for claim 1 wherein said cooling water system is a recirculating cooling water system.
4. The method of claim 1 wherein said cooling water system operated in a temperature range of from about 60° F to about 200° F.
5. The method of claim 1 further comprising added biocides, scale inhibitors, chelants, sequestering agent, dispersing agents and mixtures thereof to said cooling water system.
6. The method of claim 1 wherein from about 1 ,000 ppm to about 6,000 ppm of said alkylalkanolamine is added to said cooling water system.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US81985806P | 2006-07-11 | 2006-07-11 | |
US60/819,858 | 2006-07-11 |
Publications (2)
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WO2008006855A2 true WO2008006855A2 (en) | 2008-01-17 |
WO2008006855A3 WO2008006855A3 (en) | 2008-05-29 |
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PCT/EP2007/057115 WO2008006855A2 (en) | 2006-07-11 | 2007-07-11 | Inhibition of corrosion in cooling water system |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012021215A (en) * | 2010-07-16 | 2012-02-02 | Kurita Water Ind Ltd | Anticorrosive for boiler |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012021215A (en) * | 2010-07-16 | 2012-02-02 | Kurita Water Ind Ltd | Anticorrosive for boiler |
CN103038393A (en) * | 2010-07-16 | 2013-04-10 | 栗田工业株式会社 | Anticorrosive for boiler |
EP2594663A1 (en) * | 2010-07-16 | 2013-05-22 | Kurita Water Industries Ltd. | Anticorrosive for boiler |
EP2594663A4 (en) * | 2010-07-16 | 2014-01-01 | Kurita Water Ind Ltd | Anticorrosive for boiler |
US8728392B2 (en) | 2010-07-16 | 2014-05-20 | Kurita Water Industries Ltd. | Method of using an amine compound as anticorrosive for a boiler |
CN103038393B (en) * | 2010-07-16 | 2015-08-19 | 栗田工业株式会社 | Anticorrosive for boiler |
KR101787457B1 (en) | 2010-07-16 | 2017-10-18 | 쿠리타 고교 가부시키가이샤 | Anticorrosive for boiler |
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