Anticorrosive for boiler
a technology for anticorrosion and boilers, applied in the direction of corrosion diminishing boiler components, specific water treatment objectives, other chemical processes, etc., can solve the problems of phosphate salt hiding phenomenon or alkali corrosion, increasing the amount of organic substances unintentionally transferred to the boiler tank, and reducing the ph of the boiler water. achieve the effect of effective maintenance of the ph prevent the corrosion of the boiler tank, and high thermal stability
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[0032]The present invention will next be described in more detail by way of examples, which should not be construed as limiting the invention thereto.
[0033]In the Examples, compound (A) was 2-(2-aminoethoxy)ethanol represented by the following formula (A), and compound (B) was 3-(3-aminopropoxy)propanol represented by the following formula (B).
NH2—(CH2)2—O—(CH2)2—OH (A)
NH2—(CH2)3—O—(CH2)3OH (B)
experiment 1
[0034]A corrosion test was carried out through employment of a test boiler which was operated under the following conditions: a pressure of 4 MPa, a blow rate of 1%, a condensate recovery of 20%, pure water (ion-exchange water) feed, and use of a heater-degasser [outlet degassing capacity (dissolved oxygen level: DO) of 0.03 mg / L]. In the corrosion test, to feed water, sodium phosphate having an Na / PO4 mole ratio of 2.7 was added in an amount of 0.1 mg / L as phosphate ion, and monoisopropanolamine (MIPA) was added in an amount of 1.5 mg / L. As a result, the pH of boiler water was 10.0.
[0035]When a microamount of organic matter originating from feed water is thermally decomposed in boiler water, an organic acid is conceivably formed. Thus, 0.06 mg / L of acetic acid was added to feed water as the organic acid. In this case, the pH (25° C.) of boiler water was lowered to 9.2, lower than 9.4, which the lower limit of JIS standard value under such a pressure (Comparative Example 1). Then, M...
experiment 2
[0037]To a test boiler, pure water (ion-exchange water) having a dissolved oxygen concentration of 0.010 mg / L after degassing was fed. The boiler was operated at a pressure of 11 MPa and a blow rate of 1%, without recovering condensate. In the Comparative Examples, the boiler was operated while each of monoethanolamine (MEA), MIPA, MDEA, and 3-methoxypropylamine (MOPA) was added in an amount of 1.5 mg / L. When the pH of boiler water was stabilized, measurement was performed (Comparative Examples 3 to 6). In the Examples, the boiler was operated while the compound (A) or (B) was added in an amount of 1.5 mg / L. When the pH of boiler water was stabilized, measurement was performed (Examples 2 and 3). Table 2 shows the results.
[0038]As is clear from Table 2, in Examples 2 and 3, in which compounds (A) and (B) were added, a higher pH elevating effect was attained, as compared with Comparative Examples 3 to 6.
TABLE 2Comp.Comp.Comp.Comp.Ex. 3Ex. 4Ex. 5Ex. 6Ex. 2Ex. 3AddedMEAMIPAMDEAMOPAComp...
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