Corrosion Performance of Stainless Steel and Nickel Alloys in Aqueous Sodium Hydroxide as Revealed from Cyclic Voltammetry and Potentiodynamic Anodic Polarization
Abstract:The electrochemical behavior of nickel, Inconel 600, Incoloy 800 and 316 stainless steel electrodes in different concentration of NaOH solution was investigated using the cyclic voltammetry technique (CV). All the curves in the anodic branch of the CV are characterized by anodic dissolution peak (A), passive region (B), anodic dissolution peak (C) before oxygen evolution. In the case of the cathodic branch of CV there is one reduction peak (D) in case of Ni electrode but there are two reduction peaks (D and E)… Show more
“…The analyzed area showed an inclusion of about 29.7 µm 2 . This was also confirmed by the studies done by Abdallah et al [6][7][8] that showed the extent of pitting corrosion of the Inconel 600™ alloy when exposed to various acids and bases and that the grain boundary precipitates would correspond to (Cr -Fe) 23 C 6 and TiN.…”
Section: Results Using Potentiodynamic Polarization Analysissupporting
confidence: 80%
“…5 The corrosion rates reported varied between 0.033 and 0.8344 mm yr -1 and were obtained in solutions that varied between 0.01 M to 10.00 M, respectively. Extensive studies in using Inconel 600™ in nitric acid and caustic soda applications were performed by Abdallah et al [6][7][8] They made use of cyclic voltammetry to investigate the formation of the passivation film and compared it to other alloys such as Incoloy 800 and 316 stainless steel.…”
Inconel 600™, an austenitic high nickel alloy, has relatively low corrosion properties and is used extensively for aerospace and nuclear engineering applications. Other applications include exposure of the material to caustic and acidic environments and possible use in prosthetic implants. Electrochemical techniques, which include potentiodynamic polarization and polarization resistance, provide a means to rapidly determine the corrosion rates and the suitability of the alloy in a specific corrosive environment. The results from these two techniques were used to determine the corrosion rates as well as other thermodynamic properties for the alloy exposed to various strong and weak acids, salt and Ringer's solution. The results showed slight differences in the corrosion rates determined by the two electrochemical techniques, with those from the polarization resistance technique being on average larger. The corrosion activation energies determined for the alloy in different solutions were indicative of the corrosion rates with some anomalies in values for results observed in the 10 % acetic acid solution. The microstructural composition of the alloy was also investigated by SEM-EDS and showed peculiar inclusions that can contribute to an acceleration of the corrosion rates.
“…The analyzed area showed an inclusion of about 29.7 µm 2 . This was also confirmed by the studies done by Abdallah et al [6][7][8] that showed the extent of pitting corrosion of the Inconel 600™ alloy when exposed to various acids and bases and that the grain boundary precipitates would correspond to (Cr -Fe) 23 C 6 and TiN.…”
Section: Results Using Potentiodynamic Polarization Analysissupporting
confidence: 80%
“…5 The corrosion rates reported varied between 0.033 and 0.8344 mm yr -1 and were obtained in solutions that varied between 0.01 M to 10.00 M, respectively. Extensive studies in using Inconel 600™ in nitric acid and caustic soda applications were performed by Abdallah et al [6][7][8] They made use of cyclic voltammetry to investigate the formation of the passivation film and compared it to other alloys such as Incoloy 800 and 316 stainless steel.…”
Inconel 600™, an austenitic high nickel alloy, has relatively low corrosion properties and is used extensively for aerospace and nuclear engineering applications. Other applications include exposure of the material to caustic and acidic environments and possible use in prosthetic implants. Electrochemical techniques, which include potentiodynamic polarization and polarization resistance, provide a means to rapidly determine the corrosion rates and the suitability of the alloy in a specific corrosive environment. The results from these two techniques were used to determine the corrosion rates as well as other thermodynamic properties for the alloy exposed to various strong and weak acids, salt and Ringer's solution. The results showed slight differences in the corrosion rates determined by the two electrochemical techniques, with those from the polarization resistance technique being on average larger. The corrosion activation energies determined for the alloy in different solutions were indicative of the corrosion rates with some anomalies in values for results observed in the 10 % acetic acid solution. The microstructural composition of the alloy was also investigated by SEM-EDS and showed peculiar inclusions that can contribute to an acceleration of the corrosion rates.
“…The chemical reactions occurring in the electrolyzer have slightly darkened the electrolyte. The use of (316 SS) electrodes would probably have prevented this (Abdallah et al, 2017).…”
The main objective of this research is to generate the hydrogen gas as a fuel and part of hydroxy gas (HHO) from the drinking water (H2O) using electrolyzing method with a different electrolytes such as sodium hydroxide (NaOH), sodium carbonate (Na2CO3), and Vinegar in HHO generator for best results, the practical examinations were done by a generator that designed and built for this purpose using plate electrodes, with a rechargeable 12-volt battery and the produced gas was measured at each case and used as a fuel for operating a small single-cylinder spark-ignition engine (Honda G 200) with taking into account the safety precautions. The results show that increasing the ratio of (NaOH) grams/liter of H2O increases the gas production, while the other two electrolytes (Na2CO3 and vinegar) are not effecting too much, and using the mixing procedure (%) of the electrolytes (NaOH with Na2CO3) and (Na2CO3 with Vinegar), it is observed that the HHO generation noticeable increases with increasing the mixing ratio of the first mixture and not too much with the second.
“…Most inhibitors are organic compounds containing heteroatoms (N, O, S), unsaturated bonds and plane conjugated systems [2][3][4][5][6][7][8][9]. They are adsorbed on the steel surface and block it, thus preventing corrosion [9].…”
The inhibition impacts of two novel synthesized green biosurfactants (B-Surf.), namely, sodium Ndodecyl asparagine (AsS) and sodium N-dodecyl arginine (ArS), on the dissolution of mild steel alloy (MS-37-2), in aqueous sodium chloride solutions was inspected using various techniques. Increased concentration of NaCl solution resulted in an increase in the corrosion rate of MS-37-2. Inhibition efficiencies of B-Surf. compounds were found to increased with increase inhibitor concentrations. The synergistic inhibition action between B-Surf. inhibitors and Zn 2+ , Al 3+ and Ce 4+ on the dissolution behavior of steel alloy in NaCl solutions was investigated and interpreted. The surface morphology of the MS-37-2 surface was observed using a scanning electron microscopy (SEM). This adsorption follows Langmuir isotherm. The evaluated thermodynamic functions supported the mechanism of physical adsorption of the inhibitors. The mechanisms of corrosion and its inhibition of MS-37-2 in NaCl solutions were interpreted.
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