ISRN CorrosionVolume 2012 (2012), Article ID 937920, 9 pagesdoi:10.5402/2012/937920

Research Article

Black Wattle Tannin As Steel Corrosion Inhibitor

Rafael Silveira Peres,¹ Eduardo Cassel,² and Denise Schermann Azambuja¹

¹Laboratório de Eletroquímica, Instituto de Química, UFRGS, Avenida Bento Gonçalves 9500, 90619-900 Porto Alegre, RS, Brazil²Departamento de Engenharia Química, Faculdade de Engenharia, PUCRS, Avenida Ipiranga 6681, 90619-900 Porto Alegre, RS, Brazil

Received 31 January 2012; Accepted 22 February 2012

Academic Editors: L. Bazzi, G. Bereket, A. Kalendová, and E. E. Oguzie

Copyright © 2012 Rafael Silveira Peres et al. 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.

In order to reduce the environmental impacts caused by chemical substances harmful to the environment and human health, the black wattle tannin can be used as an environmentally friendly corrosion inhibitor in acid and near neutral media. This paper provides information on the application of black wattle tannin as an inhibitor against the corrosion of carbon steel. The inhibition was evaluated using potentiodynamic polarization (PP) and electrochemical impedance spectroscopy (EIS) at room temperature in aerated 0.1 mol L⁻¹ Na₂SO₄ (pH 6.0 and 2.5). The black wattle tannin when used as a corrosion inhibitor is more effective at acidic pH, its efficiency being dependent on its concentration. At the higher pH value (pH 6.0), a blue-black film (ferric tannate) with a short-term protection against corrosion was formed in aerated aqueous solution. At pH 2.5, this blue-black film was not observed.

1. Introduction

Tannins comprise two different classes of polyphenolic compounds; hydrolysable and condensed tannins. The condensed tannins are found in substantial concentration in the wood and bark of several trees, for instance, black wattle [1]. The tannin extracted from the bark of the black wattle tree contains flavonoid units such as (−)-robinetinidol, (+)-catechin, and (+)-gallocatechin [2]. The flavonoid units are tree-ring flavonols with fifteen carbons. The  molecular weight of condensed tannins ranges from around 500 to over 20,000 [1–3].

The hydrolysable tannins are obtained from the fruit, pod, and wood of several trees (fruit of Terminalia chebula, pod of Caesalpinia coriaria, and wood of Castanea valonea) [1–4]. This class of tannin is made up mainly of gallic and digallic acids, which are often esterified to polyols [3], and have  molecular weights of up to 3000 [1].

Due to the OH⁻ groups in the ortho position on the aromatic rings, tannins are able to form chelates with iron and other metallic cations (e.g., copper) [5]. Yahya et al. reported the formation of ferric tannate with both condensed and hydrolysable tannins [6]. When Fe³⁺ ions react with OH⁻ groups in the orthoposition in aerated aqueous solution, a highly insoluble and blue-black complex (ferric tannate) is formed [7].

The application of tannins in corrosion studies has been investigated by several authors and their efficiency is controversial. According to Favre et al. the presence of hydrolysable tannin (gallic acid) inhibits the formation of magnetite when lepidocrocite is reduced [8, 9]. Electrochemical impedance spectroscopy (EIS) experiments performed by Galvan et al. showed no substantial increase in the polarization resistance of steel due to treatment of a rusted surface with tannins [10]. On the other hand, some authors have developed a tannin primer that exhibited excellent anticorrosive properties [11–14]. Rahim et al. found that the mangrove tannin and its flavonoid monomers are potential corrosion inhibitors for steel in acidic medium [15]. According to Ross and Francis, some of the rust is converted to more stable, inert, and adherent products [16]. These contradictory results may be due to the diversity of material used in the different studies [17, 18].

Martinez investigated the mechanism of the adsorption of mimosa tannin onto low-carbon steel in sulphuric acidic solutions. At pH 1 and 2, the value of the free energy of adsorption suggests a chemisorption mechanism. This mechanism occurs due to the formation of an adsorption bond between the oxygen lone-pair electrons of the tannin ⁻OH group and the metal surface. At pH , ferric tannate is formed and the value of the free energy of adsorption suggests a physisorption mechanism of ferric tannate adsorption onto the steel surface [19].

The aim of this study was to evaluate the anticorrosive properties of tannin extracted from the bark of the black wattle tree (Acacia mearnsii De Wild.) in 0.1 mol L⁻¹ Na₂SO₄ at pH 6.0 and 2.5 for application on carbon steel. The corrosion tests were carried out in aerated sulphate solution at room temperature, using electrochemical impedance spectroscopy (EIS) and potentiodynamic polarization (PP).

2. Experimental Procedure

2.1. Material

The tannin sample used in this work was supplied by TANAC (Montenegro, Brazil). The chemical composition of the carbon steel samples is given in Table 1. All solutions and samples were prepared with analytical grade reagent. Sulphuric acid (Synth, Brazil) was used to adjust the pH value. Sodium sulphate (VETEC, Brazil) was employed in the preparation of the electrolyte solutions.

Table 1: Chemical composition of carbon steel sample.

    Chemical composition

Element
C
Mn
P
S
Cu
Cr

wt.%
0.103
0.46
0.013
0.096
0.01
0.18

2.2. Sample Preparation and Experimental Setup

Disc-working electrodes with an area of approximately 1.0 cm² were prepared from the steel samples by cold resin (epoxy) embedding. The surface was prepared by grinding with silicon carbide paper up to grade number 1200 followed by degreasing with an acetone/chloroform mixture (1 : 1) and drying under a hot air stream.

A saturated calomel electrode ( V/NHE) was used as the reference electrode, and all potentials are referred to it. The auxiliary electrode was a Pt wire. The experiments were carried out under naturally aerated conditions at 25°C. The electrochemical measurements were performed using a potentiostat (AUTOLAB PGSTAT 30, (Echo Chemie, The Netherlands)) coupled to a frequency response analyser (FRA 2). The software used for analysis of impedance spectra was FRA 4.9 (Echo Chemie, The Netherlands). The potentiodynamic polarization curves were recording at a scan rate of 1 mVs⁻¹. The corrosion potentials () and the polarization resistances () were calculated at a scan rate of 0.1 mVs⁻¹ with potential range of  mV. This method was based on ASTM G59 [20] and ASTM G102 [21] standards.

The EIS measurements were performed in potentiostatic mode at the open circuit potential, OCP. The OCP after potential stabilization is referred to in this study as the corrosion potential, . The amplitude of the EIS perturbation signal was 10 mV, and the frequency range studied was from 10⁵ to 10⁻² Hz.

Fourier transform infrared (FTIR) analysis was performed with a Perkin Elmer Spectrum 1000 spectrometer.

3. Results and Discussion

3.1. Influence of Black Wattle Tannin Concentration

Figure 1 shows the polarization resistance () for carbon steel samples immersed for 1 day in aerated 0.1  mol L⁻¹ Na₂SO₄ solutions (pH 2.5 and 6) with different concentrations of black wattle tannin. The values were obtained from stepwise potentiostatic polarization using a single small potential step of  mV.

Figure 1: Influence of tannin concentration in the polarization resistance () for carbon steel samples immersed 1 day in aerated 0.1 mol L⁻¹ Na₂SO₄ solutions: (□) pH 2.5 medium and (●) pH 6 medium.

At concentrations of up to 2 g L⁻¹ of tannin, the values of the steel samples increase for both mediums (pH 2.5 and pH 6). Concentrations above 2 g L⁻¹ were not tested due to the presence of nondissolved black wattle tannin particles in Na₂SO₄ solutions at room temperature. Thus, in this study, the concentration of tannin used as an inhibitor was 2 g L⁻¹ in aerated 0.1 mol L⁻¹ Na₂SO₄ solution. This concentration is not very different from that reported by Rahim et al. who tested the efficiency of mangrove tannin [15, 22].

3.2. Study at pH 6.0

After one hour of immersion in aerated 0.1  mol L⁻¹ Na₂SO₄ solution (pH 6.0), a nonadherent blue-black film on the steel surface and a blue-black precipitate on the bulk of the electrolyte were observed. Some authors have attributed the formation of these blue-black products to ferric-tannate formation [23]. Fourier transform infrared (FTIR) analysis was performed in order to verify whether these blue-black products were ferric tannate.

3.2.1. Results of Fourier Transform Infrared (FTIR) Analysis

The FTIR spectrum of the black wattle tannin (Figure 2(a)) shows a broad absorption band with a maximum absorbance at 3413 cm⁻¹ which is due to the presence of hydroxyl groups [15]. Peaks occurring between 1600 and 1450 cm⁻¹ are characteristic of aromatic compounds [15]. Various peaks in the 600–1300 cm⁻¹ correspond to substituted benzene rings [15].

Figure 2: (a) FTIR spectrum of the black wattle tannin and (b) FTIR spectrum of the blue-black precipitate formed in the bulk of the electrolyte after one hour of immersion of steel in aerated 0.1 mol L⁻¹ Na₂SO₄ solution (pH 6.0) in the presence of acacia tannin.

Figure 2(b) shows the FTIR spectrum of the blue-black precipitate. The reduced intensity (11.90% to 20.02% of transmittance) of the broad peak at around 3413 cm⁻¹ shows the reduction of free OH groups [24]. These hydroxyl groups in aromatic rings enable the tannins to form ferric-tannate complexes. In this way, the formation of ferric tannate was detected. The peaks occurring at 1110 cm⁻¹ and 619 cm⁻¹ are characteristic of sulphate groups (electrolyte solution) [25, 26].

3.2.2. Potentiodynamic Polarization

The potentiodynamic polarization curves of steel immersed in aerated 0.1  mol L⁻¹ Na₂SO₄ solution (pH 6.0), in the presence and absence of tannin, were obtained from 600 mV up to and 300 mV down to after different periods of immersion (Figure 3).

(a)

(b)

(c)

Figure 3: Potentiodynamic polarization curves of steel immersed in aerated 0.1 mol L⁻¹ Na₂SO₄ solution (pH 6.0) in the presence of tannin (1) and absence of tannin (2) for (a) 1 day, (b) 3 days, and 7 days.

According to Figure 3, the anodic current densities decrease in the presence of tannin in all immersion times, while the cathodic current densities show no significant modification. The presence the black wattle tannin shifts the to more positive values in whole immersion times.

The corrosion current densities in Table 2 were calculated from the extrapolation of the anodic and cathodic Tafel lines (Figure 3). The inhibition efficiencies IE (%) were calculated by the polarization resistance according to (1) [15]: where and are the polarization resistance value with the presence and absence of black wattle tannin, respectively.

Table 2: Polarization parameters for the corrosion of carbon steel immersed in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 6.0), in the presence and absence of tannin, for different periods.

(μA cm⁻²)
(V)
(Ω cm²)
IE (%)

1 day
39.66
−0.73
486.46
91.06

1 day with tannin
0.883
−0.50
5446.0

3 days
20.52
−0.73
461.37
93.03

3 days with tannin
1.512
−0.72
6622.2

7 days
13.58
−0.75
481.21
75.74

7 days with tannin
3.241
−0.72
1984.3

The value decreases significantly in the presence of tannin during the first three days of immersion. In the seventh day, the difference between the blank and the inhibitor decreases. The inhibition efficiency remains almost constant for the first and third days, though decreased on the seventh day of immersion.

3.2.3. Electrochemical Impedance Spectroscopy (EIS)

The EIS spectra for the steel in aerated 0.1  mol L−1   Na₂SO₄ solution (pH 6.0), in the presence and absence of tannin, for different periods are shown in Figures 4 and 5.

Figure 4: Nyquist plots for steel immersed in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 6.0) for 1 day (closed triangle), 3 days (closed circle), and 7 days (closed star) in the presence of tannin; and for 1 day (open square), 3 days (open lozenge), and 7 days (open circle) in the absence of tannin.

(a)

(b)

Figure 5: Bode plots for steel immersed in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 6.0) for 1 day (closed triangle), 3 days (closed circle), and 7 days (closed star) in the presence of tannin; for 1 day (open square), 3 days (open lozenge), and 7 days (open circle) in the absence of tannin.

After 1, 3, and 7 days of immersion in the presence of tannin the plots show two time constants, one at high frequency and one at low frequency with maximum phase angles of around −20° and −45°, respectively. The evolution of the EIS spectra may be related to the adsorption of the inhibitor on the metal surface resulting in an increase in the resistance of the steel to polarization. The experimental data shown in Figures 4 and 5 were fitted using two different equivalent circuits (EC) depending on the immersion time as shown in Figure 6. The fitting quality was evaluated based on the error percentage associated with each component, showing errors smaller than 5%. The software used to simulate the EIS data was NOVA 1.7 (Echo Chemie, The Netherlands). The simulated data obtained from the fittings are given in Table 3.

Table 3: Fitting parameters used to simulate the EIS plots for steel immersed for 1, 3, and 7 days in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 6.0) in the presence and absence of tannin.

Immersion time
Chi-square
Equivalent circuit
Fitting parameters

Rs (Ω cm²)
R₁ (kΩ cm²)
Q₁ (F cm²)
n

1 day

69.2
1.85
1.4810⁻⁴
0.80

3 days

Rs(R₁Q₁)
61.4
2.13
3.0110⁻⁴
0.73

7 days
1.1 10⁻³

58.6
2.30
2.2410⁻⁴
0.78

Rs(Ω cm²)
Q₁ (F cm²)
n₁
R₁ (kΩ cm²)
Q₂ (F cm²)
n₂
R₂ (kΩ cm²)

1 day with tannin
3.1 10⁻³

64.1
2.3410⁻⁶
0.64
0.369
1.8410⁻⁴
0.57
53.7

3 days with tannin
2.610⁻³
Rs(Q₁[R₁(Q₂R₂)])
62.3
3.1010⁻⁶
0.60
0.378
1.5710⁻⁴
0.63
66.5

7 days with tannin
3.410⁻³

65.6
2.6810⁻⁶
0.60
0.112
7.8310⁻⁵
0.73
6.56

represents the ohmic resistance between the reference and working electrodes; R₁ and R₂ represent the resistance or charge transfer; Q₁   and Q₂ are the impedance related to a constant phase element (CPE) and can be attributed to electrode surface or adsorbed species; n, n₁, and n₂ represent a CPE exponent. Capacitor for , a resistor for , and a diffusion process for .

Figure 6: Equivalent electric circuits proposed to simulate the experimental data of steel immersed in 0.1 mol L⁻¹ Na₂SO₄ (pH 6.0) for (a) 1, 3, and 7 days in the absence of tannin; for (b) 1, 3, and 7 days in the presence of tannin.

The equivalent circuit (EC) proposed for fitting the EIS diagram after 1, 3, and 7 days of immersion in the presence of tannin is ([]) where represents the ohmic resistance between the reference and working electrodes, and represent the resistance or charge transfer in physical meaning [27]. The and parameters are the impedance related to a constant phase element (CPE) and can be attributed electrode surface or adsorbed species [27]. The CPE impedance takes into account the phenomena due to the surface heterogeneities. The CPE impedance is given by (2) [27]: where is the impedance and is the angular frequency. The CPE represents a capacitor for , a resistor for , and a diffusion process for .

The EC proposed for 1, 3, and 7 days in the presence of tannin has two time constants. The first constant R₁Q₁ represents the time constant of high frequency which is relative to the charge transfer reactions and double layer. The second constant represents the time constant of low frequency which is relative to the adsorption processes. For all times of immersion in the absence of tannin, the EC proposed was (R₁Q₁), which contains one time constant which is related with charge transfer reactions and double layer.

The Nyquist diagram (Figure 4) shows a small variation in the polarization resistance during the first three days of immersion in the absence of tannin. On the seventh day, there is a small increase in the resistance value which can be attributed to deposition of corrosion products on the metal surface. The values were obtained from the simulated parameters considering that, in all cases, represents the overall resistance. Thus, for the circuit, this value was obtained from the sum of and . The highest values for polarization resistance were found on the first and third day of immersion in the presence of tannin. Table 4 shows the inhibition efficiencies (IE) obtained from electrochemical impedance spectroscopy (EIS) and Potentiodynamic Polarization (PP) by (1). The IE values obtained from both methods are in agreement and show a decrease in corrosion resistance with longer immersion times. This fact can be attributed due to the inhibition mechanism at this pH value which provides a formation of nonadherent and porous ferric tannate complex layer.

Table 4: Black wattle tannin inhibition efficiencies obtained from electrochemical impedance spectroscopy (EIS) and potentiodynamic polarization (PP) in 0.1  mol L⁻¹ Na₂SO₄ solution (pH 6.0).

Potentiodynamic polarization (PP)
Electrochemical impedance spectroscopy (EIS)

IE (%)
IE (%)

1 day
91.06
96.57

3 days
93.03
96.81

7 days
75.74
65.52

3.3. Study at pH 2.5

In the case of the immersion in aerated 0.1  mol L⁻¹ Na₂SO₄ solution (pH 2.5), the formation of the blue-black ferric tannate on the steel surface and in the electrolyte was not observed. According to Martinez and Stĕrn [23], the formation of ferric tannate is not detected at this pH.

3.3.1. Potentiodynamic Polarization

The potentiodynamic polarization curves of steel immersed in aerated 0.1  mol L⁻¹ Na₂SO₄ solution (pH 2.5), in the presence and absence of tannin, were obtained from 600 mV up to and 300 mV down to after different periods of immersion (Figure 7).

(a)

(b)

(c)

Figure 7: Potentiodynamic polarization curves of steel immersed in aerated 0.1 mol L⁻¹ Na₂SO₄ solution (pH 2.5) in the presence of tannin and absence of tannin for (a) 1 day, (b) 3 days, and 7 days.

The anodic current density values decreased in the presence of tannin for all exposure periods tested. Accordingly, the corrosion potential () of the metal was shifted to a more positive value and the polarization resistance () increased in the presence of tannin as observed in Table 5. The corrosion current densities in Table 5 were calculated from the extrapolation of the anodic and cathodic Tafel lines (Figure 7). The inhibition efficiencies IE (%) were calculated by the polarization resistance according to (1).

Table 5: Polarization parameters for the corrosion of carbon steel immersed in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 2.5), in the presence and absence of tannin, for different periods.

(μA cm⁻²)
(V)
(Ω cm²)
IE (%)

1 day
103.4
−0.65
202.76
55.7

1 day with tannin
25.90
−0.60
457.58

3 days
123.73
−0.68
76.863
62.0

3 days with tannin
25.93
−0.63
202.23

7 days
122.90
−0.68
68.152
68.7

7 days with tannin
29.20
−0.63
217.72

The value decreases significantly in the presence of tannin during all days of immersion. The inhibition efficiency increases with the increases of exposure days.

3.3.2. Electrochemical Impedance Spectroscopy (EIS)

The EIS spectra for the steel immersed in aerated 0.1  mol L⁻¹ Na₂SO₄ solution (pH 2.5), in the presence and absence of tannin, at OCP, for different periods are shown in Figures 8 and 9.

Figure 8: Nyquist plots for steel immersed in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 2.5) for 1 day (closed triangle), 3 days (closed circle), and 7 days (closed star) in the presence of tannin; for 1 day (open square), 3 days (open lozenge), and 7 days (open circle) in the absence of tannin.

(a)

(b)

Figure 9: Bode plots for steel immersed in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 2.5) for 1 day (closed triangle), 3 days (closed circle), and 7 days (closed star) in the presence of tannin; for 1 day (open square), 3 days (open lozenge), and 7 days (open circle) in the absence of tannin.

The Nyquist plots (Figure 8) show a decrease in the value for steel with and an increase in the time of immersion in the aerated 0.1  mol L⁻¹ Na₂SO₄ solution (pH 2.5). In the presence of tannin, the shows the opposite behaviour (increase with increased time of immersion). This can be attributed to the kinetics mechanism of the adsorption of tannin onto the metal surface and/or the formation of corrosion products from the reaction of iron with tannin. The phase angles in the presence of tannin are higher than those in the absence of tannin, reaching a maximum value of −65° which indicates an increase in the capacitive character of the film formed.

The experimental data presented in Figures 8 and 9 were fitted using the two proposed equivalent circuits (EC) shown in Figure 10. The software used to simulate the EIS data was NOVA 1.7 (Echo Chemie, The Netherlands). The simulated data obtained from the fittings are given in Table 6.

Table 6: Fitting parameters used to simulate the EIS plots for steel immersed for 1, 3, and 7 days in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 2.5) in the presence and absence of tannin.

Immersion time
Chi-square
Equivalent circuit
Fitting parameters

Rs (Ω cm²)
R₁ (kΩ cm²)
Q₁ (F cm²)
n

1 day with tannin

48.1
1.76

0.91

3 days with tannin

49.6
2.34

0.91

7 days with tannin

Rs(R₁Q₁)
57.4
3.08

0.89

1 day without tannin

63.6
0.71

0.76

3 days without tannin

49.8
0.70

0.66

Rs (Ω cm²)
Q₁ (F cm²)
n₁
R₁ (Ω cm²)
Q₂ (F cm²)
n₂
R₁  (kΩ cm²)

7 days without tannin

Rs(R₁Q₁)(R₂Q₂)
47.2

0.74
112

0.8
0.68

represents the ohmic resistance between the reference and working electrodes; R₁and R₂ represent the resistance or charge transfer; Q₁  and Q₂  are the impedance related to a constant phase element (CPE) and can be attributed to electrode surface or adsorbed species; n, n₁, and n₂ represent a CPE exponent. Capacitor for , a resistor for , and a diffusion process for .

Figure 10: Equivalent electric circuits proposed to simulate the experimental data of steel immersed in 0.1 mol L⁻¹ Na₂SO₄ solution (pH 2.5) for (a) 1, 3, and 7 days in the presence of tannin, 1 and 3 days in the absence of tannin; for (b) 7 days in the absence of tannin.

The represents the ohmic resistance between the reference and working electrodes, and represent the resistance or charge transfer in physical meaning [27]. The and parameters are the impedance related to a constant phase element (CPE) and can be attributed to electrode surface or adsorbed species. The EC proposed for all immersion times in the presence of tannin, and for 1 and 3 days, and in the absence of tannin, was . The represents the time constant which is relative to the charge transfer reactions and double layer. For fitting, the EIS diagram for 1 day of immersion in the absence of tannin the EC used was , which has two time constants. The first constant represents the time constant of high frequency which is relative to the charge transfer reactions and double layer. The second constant represents the time constant of low frequency which is relative to the adsorption processes.

A comparison between the capacitance values obtained after 1 and 3 days of immersion in solutions with and without tannin shows that this parameter decreased in the presence of tannin, which is probably due to the adsorption of inhibitor on the metal surface. Accordingly, higher values of were found in the presence of tannin (EIS parameters in Table 6).

Table 7 shows the inhibition efficiencies (IE) obtained from electrochemical impedance spectroscopy (EIS) and potentiodynamic polarization (PP). The IE values obtained from both methods are in agreement and show an increase in corrosion resistance with longer immersion times.

Table 7: Black wattle tannin inhibition efficiencies obtained from electrochemical impedance spectroscopy (EIS) and potentiodynamic polarization (PP) in 0.1  mol L⁻¹ Na₂SO₄ solution (pH 6.0).

Potentiodynamic Polarization (PP)
Electrochemical impedance spectroscopy (EIS)

IE (%)
IE (%)

1 day
55.7
59.6

3 days
62.0
70.1

7 days
68.7
74.3

The EIS data demonstrated that at pH 2.5 a distinct behaviour was detected in the presence of tannin, with the formation of a more protective film. The inhibition mechanism of tannin at this pH value should be initially adsorbed on metal surface by electron rich centers of molecule. With increase of immersion time, a layer with adherent nature was formed. That might be a reason of increasing of inhibition efficiency with the increase of immersion time at pH 2.

4. Conclusions

(i)The inhibition action of black wattle tannin towards the corrosion of steel is dependent on the concentration of tannin added and the pH value of the electrolyte. (ii)A nonadherent ferric tannate complex was formed on the steel surface at pH 6 in the presence of black wattle tannin. (iii)Ferric tannate was not formed on the steel surface at pH 2.5 in the presence of black wattle tannin. (iv)The black acacia tannin showed the formation of a layer with a short-term protection against corrosion at pH 6. (v)The black acacia tannin showed the best performance as a corrosion inhibitor at pH 2.5. The inhibition efficiency increased in the presence of tannin. (vi)Through EIS, the characteristics and behaviour of the films formed on the steel surface can be identified more clearly. The porosity of the ferric-tannate film and the stronger capacitive character of the film formed in acid medium were identified.

Acknowledgments

The financial support for this work provided by the Brazilian Government Agency CNPq and the Laboratory of Polymer Materials of the Federal University of Rio Grande do Sul (UFRGS), which carried the FTIR analysis, is gratefully acknowledged.

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