ISRN Corrosion

Volume 2012 (2012), Article ID 916367, 5 pages

doi:10.5402/2012/916367

Research Article

Kinetics of Pitting Dissolution of Austenitic Stainless Steel 304 in Sodium Chloride Solution

M. Saadawy

Chemistry Department, Faculty of Science, Alexandria University, Ibrahimia, P.O. Box 426, Alexandria 21321, Egypt

Received 26 July 2012; Accepted 6 September 2012

Academic Editors: S. Umoren and R. Wang

Copyright © 2012 M. Saadawy. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Abstract.

The effect of addition of chloride ion on the corrosion of stainless steel 304 in Na₂SO₄ solution under constant ionic strength conditions at 30°C was studied using potential-time and potentiodynamic polarization techniques and it was found that the addition of chloride ion reduces the growth of protective passive film on the surface and increase corrosion current. The kinetics of dissolution in sodium chloride solution (0.05–0.5M) at 30°C was also studied and the kinetic rate equation was derived and was found to verify the following relationship: C Cl⁻ where .

1. Introduction

Stainless steels are corrosion-resistant iron-base alloys containing a maximum of % carbon and a minimum of 10.5% chromium by weight, this is the minimum amount of chromium that prevents the formation of rust in humid unpolluted atmospheres, hence the designation “stainless”. The high corrosion resistance of the stainless steel is attributable to the presence of thin and invisible passive film [1] characterized by stability, durability, adherence, and self-repairing. Austenitic stainless steels are an extraordinary family of stainless steel alloys that have exceptional corrosion resistance and equally impressive mechanical properties which allowed them to be used as a construction material in various aggressive environments such as heat exchanger systems, drilling platforms, wastewater treatment, and desalination plants. Factors contributing to their increased use are their long service life with low maintenance cost, ability to be recycled, and benign effect on the environment and human health. Although austenitic stainless steels show a very high corrosion resistance in many aggressive environments, they can suffer pitting corrosion in chloride environments [2]. The aggressiveness and ability of ions to initiate pitting are well known [3–5]. The most popular austenitic grades have been type 304 (containing 18% chromium, 8% nickel and also known by the UNS Number S30400). The pitting mechanism of passive 304 stainless steel (or 304 SS) in 3.5% NaCl [6] and in sulphuric acid media containing chloride ions [7] has been investigated. The aim of the present work is to study the kinetics of dissolution of 304 SS in sodium chloride solution (0.05–0.5 M) at 30°C.

2. Experimental

Potential-time and potentiodynamic polarization measurements were achieved using frequency response analyzer Gill AC instrument. Polarization measurements were carried out at scan rate of 30 mV/min. The measurements were done in an electrochemical cell with three-electrode mode; platinum sheet electrode and saturated calomel electrode (SCE) were used as counter and reference electrodes, respectively. The specimen used for constructing the working electrode was stainless steel 304 that had the chemical composition (weight %) listed in Table 1.

Table 1: Chemical composition of the specimen used for constructing the working electrode.

Element
Fe
Cr
Ni
Mn
Mo
Ti
Al
V
S
C
Cu

Wt%
71.075
18.25
8.5
0.58
1.17
0.06
0.02
0.06
0.005
0.17
0.11

The stainless steel samples were fixed in polytetrafluoro-ethylene (PTFE) rods by an epoxy resin in such a way that only one surface was left uncovered. The exposed area (1 cm²) was mechanically polished with a series of emery papers of variable grades, starting with a coarse one and proceeding in steps to the finest (800) grade. The samples were then washed thoroughly with double distilled water followed with A.R. ethanol and finally with distilled water, just before insertion in the cell.

2.1. Solution Preparation

Solids: NaCl, Na₂SO₄ are purchased from Aldrich Chemicals Company. The solutions were prepared using double distilled water. Stock solutions of 1 M Na₂SO₄ and 1 M NaCl solutions were used to prepare solutions containing 0.5 M Na₂SO₄ and the desired NaCl concentration using appropriate dilutions. The concentration of the stock solution was expressed in term of moles per dm³.

3. Results and Discussion

3.1. Effect of Addition of Chloride Ion on the Corrosion Behaviour of 304 SS in Sodium Sulphate Solution under Constant Ionic Strength Conditions at 30°C

3.1.1. Potential-Time Measurement

Figure 1 shows the open circuit potential (OCP) of 304 SS in 0.5 M Na₂SO₄ solution and in 0.47 M Na₂SO₄ containing 0.1 M NaCl at 30°C, both solutions have nearly the same ionic strength. It is evident that the OCP value is shifted to a more positive value when sodium chloride is added, it was reported [7] that this is an indication of breakdown of the protective passive film formed by sulphate ion due to addition of chloride ion since the adsorbed sulphate ions in some points are replaced by the less negative chloride ions.

Figure 1: The open circuit potential (OCP) of 304 SS in (A) 0.5 M Na₂SO₄, (B) 0.47 M Na₂SO₄ + 0.1 M NaCl at 30°C.

3.1.2. Potentiodynamic Polarization Results

Figure 2 shows the potentiodynamic polarization curves for 304 SS in 0.5 M Na₂SO₄ solution and in 0.47 M Na₂SO₄ containing 0.1 M NaCl at 30°C. These polarization curves can be divided into several potential domains [8]. The cathodic domain includes potentials below the corrosion potential, where current density determined by the cathodic reaction shows a continuous increase in the current density of the cathodic branch as the potential decreases, shifting these cathodic branches to greater current densities as NaCl is added. The next potential domain corresponds to the cathodic-anodic transition, this domain is characterized by the corrosion potential and the corrosion current density. The third domain corresponds to the anodic domain region which can be divided into three parts, in the first part, the current increases graphically followed by a small quasi-passive region in which current increases slowly due to the formation of small passive film in presence of Na₂SO₄, this passive film breaks at certain critical potential, breakdown potential or at which current returns to increase quickly in the third part of anodic domain region, this breakdown potential changes to more negative value, 941 mV, when sodium chloride is added, this means that breakdown of passive film takes place earlier in the presence of chloride ion and a higher driving force is required to keep the passive film in the presence of chloride ion.

Figure 2: Potentiodynamic polarization curves of 304 SS in (A) 0.5 M Na₂SO₄, (B) 0.47 M Na₂SO₄ + 0.1 M NaCl at 30°C.

Pistorius and Burstein [9] found that the relative solubility of metal cations in pit solution increases as ratio increases which results in the increasing of saturation solubility of metal cations and increasing dissolution rate. It is reported [10] that the propagation rate of pits in depth and width is the highest at Cl⁻/SO⁻² = 0.75.

The corrosion current density,  , was calculated from the intersection of cathodic and anodic Tafel lines and the values of the electrochemical parameters: corrosion potential, , corrosion current density, , and anodic and cathodic Tafel slopes, , for the last two solutions are shown in Table 2.

Table 2: Electrochemical polarization parameters of Stainless steel 304.

Solution
(mV/SCE)
(mV/decade)
(mV/decade)
( mA/cm²)

0.5 M Na₂SO₄
167
173.1
91.5
1.5 × 10⁻⁵

0.47 M Na₂SO₄ + 0.1 M NaCl
150
182.5
107.5
2.8 × 10⁻⁵

It is clear from Table 2 that in presence of Cl⁻, goes to more positive values and increases although ionic strength is constant due to incorporation of chloride ion in the passive film while Tafel slopes, , are not significantly changed indicating the same dissolution mechanism [11–13].

3.2. Effect of Concentration of NaCl on the Polarization Behaviour of 304 SS

Figure 3 shows the potentiodynamic polarization curves for 304 SS in NaCl solutions of different concentrations at 30°C, it is clear that increasing the concentration of NaCl affects both anodic and cathodic parts of polarization curve, shifts it to greater values of , and shifts to more negative values due to the adsorption of negative chloride ions. At the pitting or breakdown potential, current increases suddenly due to breakdown of passive film. According to the literature, the pitting potential represents the potential limit above which the formation of pitting begins [14]. The more negative the value of pitting potential is, the less resistant the metal is to pit initiation and the shorter the time required for pit initiation at potentials below is, that is, shifts to smaller (more negative) values with increasing chloride ion concentration.

Figure 3: Potentiodynamic polarization curves of 304 SS in (A) 0.1 M NaCl, (B) 0.3 M NaCl, (C) 0.5 M NaCl at 30°C.

It is reported [15, 16] that the breakdown (pitting) potential shows logarithmic dependence on chloride ion concentration () of the form:

where A and B are constants and depend on the type of metal and corrosive medium.

3.3. Kinetics of the Corrosion of 304 SS in NaCl Solution

In a previous work [17] It was revealed that the passive film on stainless steel 304 exists mainly in the form H₂O–Fe–H₂O and that chloride ions adsorb at certain points on the the surface forming an intermediate complex [7] which causes rapid dissolution of the passive film to take place at these points which leads to pit nucleation. When the pit nucleus attains a critical size, crystal growth takes place stably in these positions. In most areas in which no Cl⁻ is adsorbed, passivation reactions still take place. We thus propose a mechanism in which chloride ion forms an intermediate complex with the passive metal followed by successive dissolution. This type of mechanism is given by the following series of steps:

This proposed mechanism is used to derive the kinetic rate equation for the dissolution of 304 SS in sodium chloride solution (see the Appendix). The dependence of the rate of pitting corrosion on chloride ion was found to take the form:

Application of the kinetic rate equation to polarization data of 304 SS in NaCl solutions.

The corrosion rate, V, in mils per year for the dissolution of metal is related to the corrosion current density, , using the formula [16]:

So the values of can be taken as a measure of the corrosion rate, V.

Figure 4 shows the linear fit of versus concentration of chloride ion at 30°C according to (7), this is a good support of the last proposed mechanism.

Figure 4: Linear fit of corrosion current values of 304 SS with concentration of NaCl solution according to the proposed mechanism at 30°C.

4. Conclusions

Mechanism of pitting corrosion of stainless steel 304 in sodium chloride solution involves the formation of an intermediate complex of chloride ion with the passive metal followed by successive dissolution.

Appendix

The derivation of the kinetic rate equation from the sequence of reaction steps (A.1) to (A.5) as follows:

From (A.1)

From (A.2)

Therefore

From (A.9) and (A.10)

Substitute from (A.11), (A.12) into (A.7)

Introduce into rate (A.6):

At the condition that so last equation becomes

Acknowledgments

The author wishes to thank Professor Dr. Beshir Ahmed Abd El-Nabey and Prof. Dr. Ashraf Moustafa, Department of Chemistry, Faculty of Science, Alexandria University, Alexandria, Egypt for continuous support and providing advanced instruments.

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