Abstract
Many hot corrosion problems in industrial and utility boilers are caused by molten salts. The corrosion processes which occur in salts are of an electrochemical nature, and so they can be studied using electrochemical test methods. In this research, electrochemical techniques in molten salt systems have been used for the measurements of molten corrosion processes. Electrochemical test methods are described here for a salt mixture of 80%V{sub 2}O{sub 5}-20%NaSO{sub 4} at 540-680 degree centigree. To establish better the electrochemical corrosion rate measurements for molten salt systems, information from electrochemical potentiodynamic polarization curves, such as polarization resistance and Tafeol slopes were used in this study to generate corrosion rate data. The salt was contained in a quartz crucible inside a stainless retort. The atmosphere used was air. A thermocouple sheathed with quartz glass was introduced into the molten salt for temperature monitoring and control. Two materials were tested in the molten mixture: SA213-T22 and SA213-TP347H steels. The corrosion rates values obtained using electrochemical methods were around 0.58-7.14 mm/yr (22.9-281 mpy). The corrosion rate increase with time. (Author) 7 refs.
Citation Formats
Almeraya, F, Martinez-Villafane, A, Gaona, C, Romero, M A, and Malo, J M.
Hot corrosion of the steel SA213-T22 and SA213-TP347H in 80% V{sub 2}O{sub 5}-20%Na{sub 2}SO{sub 4} mixture; Corrosion por depositos salinos de los aceros SA213-T22 y SA213-TP347H en presencia de una mezcal 80%V{sub 2} O{sub 5}-20%Na{sub 2}SO{sub 4}.
Spain: N. p.,
1998.
Web.
Almeraya, F, Martinez-Villafane, A, Gaona, C, Romero, M A, & Malo, J M.
Hot corrosion of the steel SA213-T22 and SA213-TP347H in 80% V{sub 2}O{sub 5}-20%Na{sub 2}SO{sub 4} mixture; Corrosion por depositos salinos de los aceros SA213-T22 y SA213-TP347H en presencia de una mezcal 80%V{sub 2} O{sub 5}-20%Na{sub 2}SO{sub 4}.
Spain.
Almeraya, F, Martinez-Villafane, A, Gaona, C, Romero, M A, and Malo, J M.
1998.
"Hot corrosion of the steel SA213-T22 and SA213-TP347H in 80% V{sub 2}O{sub 5}-20%Na{sub 2}SO{sub 4} mixture; Corrosion por depositos salinos de los aceros SA213-T22 y SA213-TP347H en presencia de una mezcal 80%V{sub 2} O{sub 5}-20%Na{sub 2}SO{sub 4}."
Spain.
@misc{etde_613900,
title = {Hot corrosion of the steel SA213-T22 and SA213-TP347H in 80% V{sub 2}O{sub 5}-20%Na{sub 2}SO{sub 4} mixture; Corrosion por depositos salinos de los aceros SA213-T22 y SA213-TP347H en presencia de una mezcal 80%V{sub 2} O{sub 5}-20%Na{sub 2}SO{sub 4}}
author = {Almeraya, F, Martinez-Villafane, A, Gaona, C, Romero, M A, and Malo, J M}
abstractNote = {Many hot corrosion problems in industrial and utility boilers are caused by molten salts. The corrosion processes which occur in salts are of an electrochemical nature, and so they can be studied using electrochemical test methods. In this research, electrochemical techniques in molten salt systems have been used for the measurements of molten corrosion processes. Electrochemical test methods are described here for a salt mixture of 80%V{sub 2}O{sub 5}-20%NaSO{sub 4} at 540-680 degree centigree. To establish better the electrochemical corrosion rate measurements for molten salt systems, information from electrochemical potentiodynamic polarization curves, such as polarization resistance and Tafeol slopes were used in this study to generate corrosion rate data. The salt was contained in a quartz crucible inside a stainless retort. The atmosphere used was air. A thermocouple sheathed with quartz glass was introduced into the molten salt for temperature monitoring and control. Two materials were tested in the molten mixture: SA213-T22 and SA213-TP347H steels. The corrosion rates values obtained using electrochemical methods were around 0.58-7.14 mm/yr (22.9-281 mpy). The corrosion rate increase with time. (Author) 7 refs.}
journal = []
issue = {1}
volume = {34}
journal type = {AC}
place = {Spain}
year = {1998}
month = {Jun}
}
title = {Hot corrosion of the steel SA213-T22 and SA213-TP347H in 80% V{sub 2}O{sub 5}-20%Na{sub 2}SO{sub 4} mixture; Corrosion por depositos salinos de los aceros SA213-T22 y SA213-TP347H en presencia de una mezcal 80%V{sub 2} O{sub 5}-20%Na{sub 2}SO{sub 4}}
author = {Almeraya, F, Martinez-Villafane, A, Gaona, C, Romero, M A, and Malo, J M}
abstractNote = {Many hot corrosion problems in industrial and utility boilers are caused by molten salts. The corrosion processes which occur in salts are of an electrochemical nature, and so they can be studied using electrochemical test methods. In this research, electrochemical techniques in molten salt systems have been used for the measurements of molten corrosion processes. Electrochemical test methods are described here for a salt mixture of 80%V{sub 2}O{sub 5}-20%NaSO{sub 4} at 540-680 degree centigree. To establish better the electrochemical corrosion rate measurements for molten salt systems, information from electrochemical potentiodynamic polarization curves, such as polarization resistance and Tafeol slopes were used in this study to generate corrosion rate data. The salt was contained in a quartz crucible inside a stainless retort. The atmosphere used was air. A thermocouple sheathed with quartz glass was introduced into the molten salt for temperature monitoring and control. Two materials were tested in the molten mixture: SA213-T22 and SA213-TP347H steels. The corrosion rates values obtained using electrochemical methods were around 0.58-7.14 mm/yr (22.9-281 mpy). The corrosion rate increase with time. (Author) 7 refs.}
journal = []
issue = {1}
volume = {34}
journal type = {AC}
place = {Spain}
year = {1998}
month = {Jun}
}