Available online at www.sciencedirect.com Scripta Materialia 62 (2010) 45–48 www.elsevier.com/locate/scriptamat In situ surface investigation of austenitic stainless steel in nitric acid medium using electrochemical atomic force microscopy N. Padhy, S. Ningshen, U. Kamachi Mudali* and Baldev Raj Corrosion Science and Technology Division, Indira Gandhi Center for Atomic Research, Kalpakkam 603102, Tamil Nadu, India Received 7 August 2009; revised 19 September 2009; accepted 19 September 2009 Available online 24 September 2009 Using potentiodynamic polarization and electrochemical atomic force microscope, the surface morphology of austenitic stainless steel has been investigated with the aim of understanding the passive film property in nitric acid medium. It has been found that passive film consists of platelet-like structures with a moiré pattern at lower concentrations (0.1, 0.5 M); at higher concentrations (0.6, 1 M) the platelet-like structures disappear, revealing the grain boundary structure. Ó 2009 Acta Materialia Inc. Published by Elsevier Ltd. All rights reserved. Keywords: Stainless steels; Atomic force microscope; Corrosion; Grain boundaries; Surface morphology Austenitic stainless steels (SS) of type 304L SS are used at different concentrations and temperatures of HNO3 in nuclear fuel reprocessing plants due to their good passivation property, high corrosion resistance and good mechanical property [1–3]. However, certain corrosion problems have been observed, depending on the concentration of HNO3 acid, the presence of redox electrochemical species and the temperature, leading to degradation in the corrosion resistance of components and pipings of type 304L SS [1,2]. 304L SS is indispensable for successful fuel reprocessing application due its affordable cost, fabricability and availability, thus a detailed fundamental study to understand the corrosion aspects in nitric acid medium is demanded. A number (albeit small) of significant attempts have been made to comprehend the phenomenon of localized corrosion in stainless steel in various electrochemical environments using an in situ scanning probe technique. Kamachi Mudali and Katada [4] investigated the nanomechanical properties of passive film of 304LN SS and predicted a decrease in stiffness value and increase in height of passivated surface in 0.5 M NaCl medium under different surface conditions. Williford et al. [5] studied pitting and intergranular corrosion of 304 SS in NaCl and oxalic acid medium, and demonstrated the growth of pit and initiation of intergranular corrosion. Zhang et al. [6] analyzed the role of corrosion products * Corresponding author. Tel.: +91 44 27480121; fax: +91 44 27480301; e-mail: [email protected] on pitting corrosion of SUS 304 SS and reported that the current density for the pit growth is higher than that of the applied current. However, to our knowledge, no in situ study has been carried out to date to understand the process of corrosion in austenitic stainless steel in HNO3 medium which is a major concern in spent nuclear fuel reprocessing plants. The aim of the present work is to understand the in situ surface morphology of 304L SS in HNO3 medium using an electrochemical atomic force microscope (EC-AFM). Specimens of dimensions 10 10 1.6 mm were cut from a sheet of 304L SS and solution annealed at 1323 K for 30 min. The specimens were mechanically polished in SiC emery sheet up to 1400 grade and then polished in diamond paste (0.25 lm) to get a mirror-like finish. Finally, all the polished specimens were ultrasonically cleaned in acetone and double-distilled water. Potentiodynamic anodic polarization study was carried out to understand the polarization behavior of 304L SS in 0.1, 0.5, 0.6 and 1 M HNO3. Polarization tests were conducted at room temperature using a Solartron 1287 electrochemical interface associated with a standard three-electrode cell comprising Pt as the counter electrode, Ag/AgCl as the reference electrode and the sample as the working electrode. The test solution was not deaerated as the experiments were carried out to simulate the plant condition. Five sets of experiments were carried out for each concentration to check the reproducibility. Corrosion potential (Ecorr) and corrosion current density (Icorr) were calculated by the Tafel extrapolation method by fitting Tafel lines in the close 1359-6462/$ - see front matter Ó 2009 Acta Materialia Inc. Published by Elsevier Ltd. All rights reserved. doi:10.1016/j.scriptamat.2009.09.026 46 N. Padhy et al. / Scripta Materialia 62 (2010) 45–48 vicinity (100 mV) of the corrosion potential. Passive current density (Ipass) is the current density in the passive range of type 304L SS at a particular concentration, and the transpassive potential (Etranspass) was determined at the potential where the anodic current increased monotonically to exceed the mean passive current density. The range of anodic current for determination of the transpassive potential was 65–150 lA. The quantitative values given for the corrosion related parameters are the mean of all the tests carried out in a particular solution, with the standard deviation given to indicate the accuracy. An in situ surface morphological investigation in the aforementioned HNO3 concentrations at a fixed location of the specimen (without changing the specimen position) was carried out using an EC-AFM (Solver Pro EC, NTMDT, Moscow) in ambient conditions with potentiostatic control to monitor the sequential morphological changes occurring over the surface. Like the polarization study, the solution was not deaerated. The electrochemical cell is made up of Teflon and has a volume capacity of 5 ml. It consists of Pt as the counter electrode, Ag/AgCl as the reference electrode and the sample as the working electrode. Prior to measurement, the bipotentiostat was calibrated for the applied and measured potential ranges. Similarly, the scanner used was also calibrated using standard grating. All the morphological measurements were carried out in semi-contact mode using a conical silicon tip having a force constant of 5 nN m1 with a frequency range of 50–150 Hz and a cone angle of less then 22°. The potential for the in situ study was varied from the cathodic to the anodic region, based on the polarization curve obtained, at a step of 50 mV vs. Ag/AgCl, and by holding at that potential for 10 min. The results for anodic polarization study are as shown in Figure 1. The polarization plots did not reveal any active–passive transition behavior, as after the cathodic region it quickly entered into the passive region over a wide potential range, followed by the transpassive regime. The quantitative values of all the corrosion related parameters are given in Table 1. The maximum standard deviations for Ecorr, Icorr, Ipass and Etranspass for all the concentrations of HNO3 given in Table 2 were within ±6 mV vs. Ag/AgCl, ±5 103 lA cm2, ±3 lA cm2 Potential (V) Vs Ag/AgCl 2.0 1.5 0.1 M HNO3 0.5 M HNO3 0.6 M HNO3 1 M HNO3 1.0 0.5 0.0 -0.5 -1.0 -2 10 -1 10 0 10 1 10 2 3 10 10 4 10 2 Log Current density (µ A/cm ) Figure 1. Potentiodynamic polarization behavior of 304L SS in 0.1, 0.5, 0.6 and 1 M HNO3. and ±27 mV vs. Ag/AgCl, respectively. By going from the lowest to the highest concentration, the results revealed that Ecorr increased by 50 mV vs. Ag/AgCl, Icorr increased by two orders of magnitude, Ipass increased by one order of magnitude and Etranspass decreased by around 150 mV vs. Ag/AgCl. It is well known that the reduction of nitric acid is autocatalytic in nature, with the generation of aqueous HNO2 and gaseous species such as NO and NO2 depending on the concentration used [3,7]. With increasing nitric acid concentration, the reduction rate, and thus the oxidizing power, also increases as the ratio of nitrous acid to nitric acid increases. Thus, from a kinetics point of view, the generation of nitrous acid, which maintains the autocatalytic nature, accelerates the corrosion rate due to the oxidation of alloying elements such as Fe and Cr. Consequently, chromium, which is key to passive film stability, depletes from the surface, leading to an increase in the corrosion potential, and increases in the passive current density and corrosion current density. Similarly, owing to the higher catalytic activity at higher concentrations, the transpassive dissolution of passive film also becomes faster, leading to a decrease in the tranpassive potential. The results for the in situ surface morphology study of type 304L SS in 0.1, 0.5, 0.6 and 1 M HNO3 at 1100 mV vs. Ag/AgCl are presented in Figure 2(a–d). The justification for showing the morphology at 1100 mV is that this is the best passive condition at all the concentrations, and contrasting surface features were observed clearly at this potential in all the concentrations. Figure 2a represents the surface morphology inside the solution at 1100 mV in 0.1 M HNO3, Figure 2b represents the surface morphology at 1100 mV in 0.5 M HNO3, Figure 2c represents the surface morphology at 1100 mV in 0.6 M HNO3 and Figure 2d represents the surface morphology at 1100 mV in 1 M HNO3. As can be seen from Figure 2a, in 0.1 M HNO3 the surface is covered with platelet-like structures [8] in the form of moiré pattern, i.e. there is a successive formation of layer structures. This type of growth mode of the platelets has been correlated with the growth of the oxide layer by Vignal et al. [8] using a limited height method by plotting the platelets’ mean area vs. Z-height. The surface morphology in 0.5 M HNO3 (Fig. 2b) at 1100 mV also shows the formation of the platelet-like structures; however, the size of the platelets is smaller compared to in 0.1 M HNO3. The platelets’ projected area (AS), the inclination (h) between adjacent layers, the disorientation angle (u) between platelets in the same layer and the root mean square roughness (Rq) value for 0.1 and 0.5 M were calculated using NOVA software, and are presented in Table 2. The size of the platelets was determined as rectangular grains, the inclination (h) was determined by taking three platelets (two in the same layer and the third in an adjacent layer), the disorientation angle was determined by taking three platelets in the same layer (top to bottom) and the root mean square roughness was determined by using Eq. (1): sffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi Pn i¼1 ðZ i ZÞ Rq ¼ ð1Þ n N. Padhy et al. / Scripta Materialia 62 (2010) 45–48 47 Table 1. Polarization parameters for 304L SS in 0.1, 0.5, 0.6 and 1 M HNO3. Conc. of HNO3 (M) Ecorr (mV vs. Ag/AgCl) Icorr (lA cm2) Ipass (lA cm2) Etranspass (mV vs. Ag/AgCl) 0.1 0.5 0.6 1 125 100 97 75 1.35 101 7.50 101 1.01 101 1.65 101 6 101 9.5 101 11 101 1.45 102 1400 1345 1330 1250 Table 2. Statistical EC-AFM data for 0.1, 0.5, 0.6 and 1 M HNO3. Conc. of HNO3 (M) AS (lm2) h (deg) u (deg) Rq (nm) 0.1 0.5 0.6 1 0.8–1 0.4–0.7 – – 45–65 10–20 – – 2 1 – – 9 6 4 20 where Zi is the height value of each single point, Z is the mean of all the height values and n is the number of data points within the image. From Table 2, it is evident that the size of the platelet, the angle of inclination, the disorientation angle and the root mean square roughness value decreased with increasing HNO3 concentration, giving a uniform and smooth morphology at 0.5 M HNO3. The interesting feature in both 0.1 M and 0.5 M HNO3 is that no visible corrosion process was observed on the surface, with the surface being covered fully by the platelets. The morphology in 0.6 M HNO3 is quite interesting and different from that in both 0.1 and 0.5 M HNO3. Both the formation of platelet-like structures and the initiation of the surface dissolution process were observed. However, the platelets formed were very few in number, and the surface dissolution occurred at the brighter regions of the surface, which are the elevated portions. The morphology in 1 M HNO3 is totally different as compared to those in 0.1, 0.5 and 0.6 M HNO3. In 1 M HNO3 the formation of plateletlike structures was not observed at all; instead, grain boundaries opened up at a potential of 1100 mV. At higher concentrations of HNO3, the oxidizing power increases, which preferentially attacks oxide boundaries as these are the high-energy regions. Overall, the in situ results demonstrate the formation and breakdown of passive film with increasing oxidizing power of nitric acid. According to the passivation model for austenitic stainless steel in acidic media [9], passive film is a gel-like structure, which starts decaying in an aggressive electrochemical environment and eventually breaks down where local inhomogenities expose a small amount of the surface, thereby initiating surface dissolution. In the present investigation, a decrease in surface roughness value was observed from the surface morphology study up to 0.6 M HNO3. The decaying of the passive film is supported by the decrease in roughness value, as the height of the passivated surface is correlated with the roughness of the surface [4]. The decrease in roughness from 0.1 to 0.6 M HNO3 is due to thinning of the passive film, which symbolizes the start of the decay nature. Supportive evidence for the breakdown of passive film and the initiation of surface dissolution is apparent from the morphology at 0.6 M HNO3, where surface dissolution is observed in the presence of platelet-like structures. However, towards higher concentrations (1 M) the increase in roughness (20 nm) is due to the increase in the surface dissolution process and the opening up of oxide boundaries. Figure 2. Surface morphology of 304L SS at 1100 mV in (a) 0.1 M HNO3, (b) 0.5 M HNO3, (c) 0.6 M HNO3 and (d) 1 M HNO3. 48 N. Padhy et al. / Scripta Materialia 62 (2010) 45–48 In summary, this investigative study on the surface of austenitic stainless steel in nitric acid medium using an electrochemical atomic force microscope revealed that platelet-like structures formed in lower concentrations (0.1, 0.5 M) of HNO3, providing effective protection for the surface, but cease to form at concentrations beyond 0.6 M HNO3, when grain boundaries are revealed and selective dissolution starts. [1] Baldev Raj, U. Kamachi Mudali, Prog. Nucl. Energy 48 (2006) 283–313. [2] U. Kamachi Mudali, R.K. Dayal, J.B. Gnanamoorthy, J. Nucl. Mater. 203 (1993) 73–82. [3] S. Ningshen, U. Kamachi Mudali, G. Amarendra, Baldev Raj, Corros. Sci. 51 (2009) 322–329. [4] U. Kamachi Mudali, Y. Katada, Electro. Acta 46 (2001) 3735–3742. [5] R.E. Williford, C.F. Windisch Jr., R.H. Jones, Mater. Sci. Eng. A288 (2000) 54–60. [6] Q. Zhang, R. Wang, M. Kato, K. Nakasa, Scripta Mater. 52 (2005) 227–230. [7] P. Fauvet, F. Balbaud, R. Robin, Q.-T. Tran, A. Mugnier, D. Espinoux, J. Nucl. Mater. 375 (2008) 52–64. [8] V. Vignal, J.C. Roux, J.M. Olive, D. Desjardins, V. Genton, Acta Mater. 46 (1998) 149–157. [9] G. Okamoto, Corros. Sci. 13 (1973) 471–489.
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