Research Article, J Nucl Ene Sci Power Generat Technol Vol: 6 Issue: 4
Influence of Aluminum Addition on the Corrosion of 304 Stainless Steel in High Temperature Water
Xiao-Fang Song*, Sheng-Han Zhang and Ke-Gang Zhang
School of Environmental Science & Engineering, North China Electric Power University, Baoding 071003, Hebei Province, P. R. China
*Corresponding Author : Xiao-Fang Song
School of Environmental Science & Engineering, North China Electric Power University, Baoding 071003, Hebei Province, P. R. China
E-mail: [email protected]
Received: October 30, 2017 Accepted: November 08, 2017 Published: November 15, 2017
Citation: Song F, Zhang S, Zhang K (2017) Influence of Aluminum Addition on the Corrosion of 304 Stainless Steel in High Temperature Water. J Nucl Ene Sci Power Generat Technol 6:4. doi: 10.4172/2325-9809.1000178
The influence of Al3+ addition on the corrosion of 304 stainless steel (SS) in high temperature water has been investigated by gravimetric analysis, potentiodynamic polarization and Mott-Schottky plots. After Al3+ addition, the amount of oxidized metal on 304 SS was reduced, the open circuit potential was shifted towards positive direction, the passive current density was declined, and the donor density of the oxide film formed on 304 SS surface was decreased. The corrosion kinetics of 304 SS in this work was curved to be parabolic with a 25% reduction of the parabolic rate constant by Al3+ addition. The activation energy of the corrosion process was increased due to the presence of Al which slowed down the 304 SS corrosion. The structure and composition of oxide film formed on 304 SS in high temperature water may be changed by Al3+ addition. The work may give a decent route for radiation field or consumption control in the essential circuit water of PWR.
Keywords: Aluminum addition; 304 Stainless steel; Pressurized water reactor; Corrosion kinetics; Oxide film
A 304 stainless steel (SS) has been widely used as structural material in many nuclear power plants for its excellent mechanical properties, especially for its corrosion resistance. In general, the corrosion rate of 304 SS in nuclear reactor coolant system is very slow. Even so, the transmitting and activation of corrosion products must be taken seriously [1,2]. The presence of 60Co in the primary circuit water of pressurized water reactor (PWR) is one primary cause which aggravates the corrosion of material and radiation build-up. Zn addition technology was often used for radiation field and corrosion control, which may change the composition and structure of oxide film formed on 304 SS [3,4]. 60Co in the spinel oxides formed on stainless steel may be replaced by Zn2+, which may reduce the corrosion speed of 304 SS and the dose rate of Co . However, natural zinc could be activated into 65Zn which may also result in radiation build-up . Along these lines, the costly drained Zinc rather than regular zinc was utilized which implies a much high cost. Some ease innovation is required for the erosion and radiation develop control in Nuclear power plants. Aluminum (Al3+) expansion might be a decent decision which can diminish the consumption of the 304 SS and 316 SS in the bubbling water reactor (BWR) essential coolant while the normal Al isotopes won’t bring about the radiation field develop . In this study, the influence of Al3+ addition on the corrosion behavior of 304 SS has been investigated in the simulated primary circuit water of pressurized water reactor (PWR).
The chemical composition of the 304 SS used in the present work was listed as follows (wt, %): 0.045 C, 0.63 Si, 1.10 Mn, 8.06 Ni, 19.57 Cr and balance Fe. The 304 SS specimens (12 mm ×10 mm × 2 mm) were mechanically ground in turn with 400, 600, 800, 1200, 1500 and 2000-grit silicon carbide papers and then mechanically polished with alumina gel (0.5 μm). The specimens were ultrasonically cleaned by ethanol and pure water in sequence. Then the specimens were dried with cold wind and then measured for the precise dimension and weight. All the specimens were kept in the dry vessel for use.
The specimens were exposed in the simulated primary circuit water of PWR contained in a 1 L stainless steel autoclave. The simulated solutions contained 1200 mg/L H3BO3 (counted as B), 2.2 mg/L LiOH∙H2O (counted as Li) and 2 mg/L (CH3COO)2Co∙4H2O (counted as Co, 59Co instead of 60Co) with or without 0.1 mg/L (CH3COO)3Al (counted as Al). Before exposure, the aqueous solutions were deaerated by continuous bubbling with nitrogen gas for 2 h. Test specimens were exposed in the above aqueous environment at 473.15 K, 523.15 K and 553.15 K, respectively. The examples after introduction were cleaned and cooled, and afterward put away in the dry vessel for utilize.
The specimens (triplicate corrosion specimens) after exposure were descaled using a two-step alkaline permanganate/ammonium citrate process: (1) 3% KMnO4 and 10% NaOH for 5 min boiling followed by wiping and (2) 10% (NH4)2HC6H5O7 for 5 min boiling. This ideal descaling arrangement was dictated by analyze and the strategy for concoction descaling alludes to ASTM G1-03. The descaled examples were ultrasonically cleaned by ethanol and unadulterated water. The specimens were all dried to a constant weight. The descaled weight-loss of 304 SS specimen was calculated by Eq. 1:
Here, w0 is the weight of specimen before exposure (mg), w1 is the weight of specimen after descaling (mg), and S is the superficial area of the specimen (dm2).
The electrochemical experiments were carried out by a classical three-electrode cell. A platinum counter electrode and a saturated calomel reference electrode (SCE, all potential values mentioned refer to) were employed in the three-electrode cell. The exposed specimens were used as the working electrode which was encapsulated by polytetrafluoroethylene (PTFE) tape with a 0.2826 cm2 window exposed. Fresh exposed specimen was used in each electrochemical experiment. All measurements were performed at room temperature in the borate buffer solutions (0.15 mol/L boric acid, 0.0375 mol/L sodium borate, pH=8.4) with Parstat 2273.
Potentiodynamic polarization and Mott-Schottky plots were utilized to examine electrochemical attributes of oxide films on 304 SS after high temperature presentation. The potentiodynamic polarization tests were performed at 1 mV/s checking rate. The capacitance experiments (Mott-Schottky plots) were performed at 1 kHz frequency and with 10 mV intervals in the potential range from 0.2 to -0.4V.
Results and Discussion
Table 1 summarizes the amounts of descaled weight losses on 304 SS specimens after exposure. The descaled weight loss of 304 SS specimen represents the total amount of the oxidized metals on 304 SS. It shows that the weight loss (oxidized metal) of 304 SS increases significantly with the temperature increases. It indicates that the corrosion resistance of 304 SS decreases in high temperature solution. It must be illustrated that weight loss of 304 SS is reduced by Al3+ addition into the simulated solution. This indicates that Al3+ addition reduces the oxidation of 304 SS and strengthens its corrosion resistance.
|Time [h]||Δw [mg·dm-2]|
|473.15[K]||523.15 [K]||553.15 [K]|
aAl-free solution; bAl-containing solution.
Table 1: Weight loss of 304 SS specimens exposed in various simulated solutions.
Figure 1 shows the weight loss on 304 SS specimen along with exposure time before and after Al3+ addition. The measure of oxidized metals in the underlying stage expanded forcefully which exhibits the core arrangement of oxide at the deformities of 304 SS. At that point, the expansion of oxidized metals was backed off in the center and later stages demonstrating the arrangement of an entire oxide film. The primary quick back moderate erosion rate shows the change of consumption conduct from substance response control to dissemination process control. Corrosion kinetics of 304 SS was analyzed according to the weight loss of the original specimen (Δw) accompanied by the increasing of exposure time (Figure 1).
The corrosion kinetics was fitted to the parabolic model under all reaction conditions. The corrosion kinetics can be curved by Eq. 2
Here, kp is the parabolic rate constant (mg metals∙dm-2∙h-0.5) and t is the reaction time (h). The parabolic rate at each temperature was calculated showing an increase with temperature as happened in most chemical reactions. The fitted parabolic rate constants of 304 SS exposed at 473.15, 523.15 and 553.15 K in Al-free simulated solutions are 0.862, 1.265 and 1.360 mg metals∙dm-2∙h-1/2, respectively (Figure 1a). Remarkably, the fitted parabolic rate constants of 304 SS exposed at 473.15, 523.15 and 553.15K in Al-containing simulated solutions are lowered to 0.633, 0.939 and 1.085 mg metals∙dm-2∙h-1/2, respectively (Figure 1b). The results show a significant decrease in the parabolic rate constant (about 25%) due to presence of Al3+. Such phenomenon gives a direct evidence for the inhibition behavior by Al3+ in corrosion process of 304 SS.
The Arrhenius equation is an empirical formula used in the chemical process to indicate the relationship between the reaction rate constant and the temperature change. The activation energy can be obtained by the logarithmic expression of Arrhenius equation:
Here, k is the corrosion reaction rate constant, R is the molar gas constant, Ea is the apparent activation energy of the reaction, T is the thermodynamic temperature, and A is the frequency factor. Ea is the energy needed when a reactant molecule transforms into a corrosion product. Hence, activation energy in the whole general corrosion process is introduced as a sensitivity indicator for initiation of corrosion on 304 SS under different temperatures. Ea can be calculated according to the slope of the plot of lnk versus 1/T. The slope values are listed in Table 2. It shows that the activation energy of 304 SS in corrosion process is increased by Al addition, and the corrosion of 304 SS is slowed down. The relatively low values of activation energy may be attributed to the comparatively high temperature that used in this research (473.15-553.15K). It likewise might be clarified by that recurrence factor overwhelms the erosion rate when the consumption is controlled by dispersion process. At that point, the expansion of oxidized metals was backed off in the center and later stages demonstrating the arrangement of an entire oxide film. The primary quick back moderate erosion rate shows the change of consumption conduct from substance response control to dissemination process control . The aluminum ions addition may change the structure of the oxide film formed on 304 SS which blocks the micropore diffusion of the metal ions.
Table 2: Ea of the corrosion process on 304 SS in the Al-free and Al-Containing solutions.
Figure 2 shows the potentiodynamic polarization curves of the 304 SS specimens after 168 h exposure in the Al-free and Alcontaining solutions. No obvious passivation range was observed and the anodic current density increases continuously with the increase of potential for the 304 SS specimens exposed in the Alfree simulated solution at 523.15 and 553.15K. However, the passive current density is remarkably reduced due to the presence of Al3+ at all temperatures. Specifically, the latent potential territory is clearly seen in the potentiodynamic polarization of the example uncovered in the Al-containing arrangement at 523.15 and 553.15K. These all indicates that the Al3+ addition in the simulated primary circuit water of PWR can strengthen the protection of 304 SS from corrosion.
It is well established that corrosion performance of material is closely related with their semiconductor properties [9,10]. Semiconductor is highlighted by its low electron focus. At the point when a semiconductor is placed in a solution and the electron exchange between the two stages achieves equilibrium, a space charge layer (or an exhaustion layer) will be framed in favor of the oxide film in the interface district and a Helmholtz layer will be shaped in favor of the electrolyte. Under the fixed 1 kHz frequency of Parstat 2273 in this experiment, the Helmholtz layer capacitance can be neglected and the measured capacitance is equal to the space charge layer capacitance [11,12]. The relationship between the space charge capacitance (C) and the applied potential (E) is obtained by the Mott- Schottky equation for n-type semiconductor (Eq.4):
here ε is the dielectric constant of the oxide film, usually taken as, ε0 is the vacuum permittivity (8.854×10-14 F/cm), e is the electron charge (1.602×10-19 C), ND is the donor density, Efb is the flat band potential, k is the Boltzmann constant (1.38×10-23 J/K), and T is the absolute temperature. ND can be calculated from the slope of the C-2 versus E curve. Figure 3 shows the Mott-Schottky plots of 304 SS after high temperature exposure in Al-free and Al-containing simulated solutions [12,13]. The slopes of the curves are positive at the range of -0.4 - 0.1 VSCE, suggesting an n-type semiconductor behavior of the oxide film on 304 SS. The ND was calculated by the slope of the fitted lines, as shown in Table 3. The donor density increases with the increase of temperature indicating the weakened corrosion resistance [10,14]. Interestingly, compared with the specimen exposed in Al-free solution, the donor density of the specimen exposed in Al-containing solution is decreased about 40% at each temperature. This suggests that the structure of oxide film can be changed by Al3+ addition which results in a stronger corrosion resistance.
|523.15 K Alfa||523.15 K Alcb||553.15 K Alfa||553.15 K Alcb|
Table 3: Donor density of oxide films on 304 SS specimen after 168 h exposure in various simulated solutions.
The effect of Al3+ addition on the corrosion of 304 SS exposed to simulated primary circuit of PWR has been investigated by potentiodynamic polarization, Mott-Schottky plots and erosion energy. Al3+ expansion in high temperature water can diminish measure of the oxidized metal, bring down the consumption activity vitality and change the semiconductor properties of the oxide film. Al3+ addition may change the structure of the oxide film formed on 304 SS. Al3+ addition will reduce the migration and activation of corrosion products by inhibiting the corrosion of the 304 SS in the primary circuit water of PWR. Al3+ water chemistry will be a good way to replace Zn water chemistry for radiation field and corrosion control.
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