[Retracted] Inhibition Effect of Substituted Thiadiazoles on Corrosion Activity of N80 Steel in HCl Solution

Yadav, M.; Kumar, Sumit; Behera, Debasis

doi:https://doi.org/10.1155/2013/256403

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Research Article | Open Access

Volume 2013 | Article ID 256403 | https://doi.org/10.1155/2013/256403

[Retracted] Inhibition Effect of Substituted Thiadiazoles on Corrosion Activity of N80 Steel in HCl Solution

M. Yadav,¹Sumit Kumar,¹and Debasis Behera¹

Academic Editor: Elena V. Pereloma

Received29 Nov 2012

Revised02 Mar 2013

Accepted18 Mar 2013

Published18 Apr 2013

Abstract

The inhibition effect of some prepared compounds, namely, thiadiazole derivatives, on N80 steel corrosion in 15% HCl solutions has been studied by using the weight loss, electrochemical polarization, and electrochemical impedance spectroscopy techniques. It was found that the inhibition efficiency of the thiadiazole derivatives, namely, 2-amino-5-(4-methoxyphenyl)-1,3,4-thiazole (AMPT), 2-amino-5-phenyl-1,3,4-thiazole (APT), and 2-amino-5-(4-chlorophenyl)-1,3,4-thiazole (ACPT), increases with the increase in concentration. Inhibition efficiency follows the order AMPT > APT > ACPT. The effect of temperature on the corrosion was investigated by the weight loss method, and some thermodynamic parameters were calculated. The inhibitive action may be attributed to the adsorption of inhibitor molecules on the active sites of the metal surface following Langmuir adsorption isotherm. Polarization measurements indicated that thiadiazole derivatives act as mixed-type corrosion inhibitor. The adsorption of thiadiazole derivatives on N80 surface exposed to inhibitor-containing solutions was confirmed using SEM and FT-IR spectra.

1. Introduction

N80 carbon steel has been generally used as the main construction material for down hole tubular, flow lines, and transmission pipelines in petroleum industry. In most industrial processes, acidic solutions are commonly used for pickling, industrial acid cleaning, acid descaling, oil well acidifying, and so forth [1–5]. It is commonly noticed that 15–28% of hydrochloric acid is used for the acidization of petroleum oil wells [6, 7]. Because of their aggressiveness, iron and its alloys get corrodes during these acidic applications particularly with the use of hydrochloric acid and sulphuric acid, which results in terrible waste of both resources and money [8]. Addition of inhibitor remains the necessary procedure to secure the metal against acid attack. Therefore, corrosion inhibitors for HCl solutions have attracted more attention. Most of the well-known corrosion inhibitors are organic compounds containing polar groups having nitrogen, sulphur, and/or oxygen atoms and heterocyclic compounds with polar functional groups and conjugated double bonds [9, 10]. These compounds can adsorb on the metal surface and partially blocking the active sites on the surface, thereby reducing the corrosion rate. Among different nitrogen- and sulphur-containing compounds, thiosemicarbazide has been reported to be a potential inhibitor for different metals [11, 12]. Most of the investigation is related to the application of common inhibitors like various derivatives of the compound of aminothiazoles [13], benzotriazoles [14–16], thioimidazole [17], mercapto-5-triazole [18], and thiadiazole [19, 20] which have been used as potential inhibitors for this system.

Keeping in the view of the above excellent behavior of the organic compounds containing nitrogen and sulphur as corrosion inhibitors, some compounds of substituted thiadiazoles, namely, 2-amino-5-(4-methoxyphenyl)-1, 3,4-thiadiazole (AMPT), 2-amino-5-phenyl-1,3,4-thiadiazole (APT), and 2-amino-5-(4-chlorophenyl)-1,3,4-thiadiazole (ACPT), have been synthesized, and their corrosion inhibition property was studied by the weight loss technique and electrochemical techniques.

2. Experimental Section

2.1. Materials

2.1.1. Composition of N80 Sample

The working electrode and specimens for weight loss experiments were prepared from oil well N80 steel having the percentage composition (wt.%) as shown in Table 1. The specimens were mechanically abraded with 320, 400, 600, 800, 1000, and 1200 emery paper, washed in acetone and double-distilled water, then dried, and put into the cell.

2.1.2. Solutions

The aggressive solutions were made up of 37% HCl (Rankem). The concentration of the used inhibitors ranged from 20 ppm to 200 ppm in 15% HCl. All solutions were prepared in double-distilled water.

2.1.3. Synthesis of Corrosion Inhibitor

The inhibitors AMPT, APT, and ACPT were synthesized in the laboratory by a reported method [21] as shown in Scheme 1. An equimolar mixture of substituted benzoic acid (0.05 mol), thiosemicarbazide (0.05 mol), and phosphorous oxychloride (15 mL) was refluxed gently for half an hour. After cooling, water was added (45 mL) and the mixture was refluxed for 4 h and filtered. The solution was neutralized with saturated solution of potassium hydroxide. The precipitate was filtered and recrystallized from ethanol. Their purity was confirmed by TLC. The structure of inhibitors is shown in Table 2.

2.2. Methods

2.2.1. Weight Loss Method

The N80 specimens were cut in the dimension of 3 cm × 3 cm × 0.1 cm with a small hole of 2 mm at the upper edge of specimen for weight loss studies, and the size of the electrodes was 1 cm × 1 cm with 4 cm long tag for electrochemical studies with an exposed area of 1 cm² towards aggressive solution. The specimens were mechanically abraded successively with 1/0, 2/0, 3/0, and 4/0 grade emery papers. The surface was thoroughly washed with soap, running tap water, and distilled water and finally was degreased with acetone. The samples were dried and stored in vacuum desiccators before immersion in the test solution. Weight loss measurements were performed at 303 K for 6 h by immersing the N80 steel coupons into 250 mL of 15% hydrochloric acid in the absence and the presence of various amounts of inhibitors. After the elapsed time, the specimens were taken out, washed, dried, and weighed accurately. The experimental studies were performed at temperature range of 303 K to 333 K. The inhibition efficiency (IE%) and surface coverage () were determined by using following equation [22]: where = weight loss (mg), = density of specimen (g/), = area of specimen (), and = exposure time (hours). The degree of surface coverage () by inhibitors can be expressed in terms of corrosion rate as where = corrosion rate in the absence of inhibitor and = corrosion rate in the presence of inhibitor.

2.2.2. Electrochemical Method

The electrochemical experiments were carried out in a three-necked glass assembly containing 250 mL of the electrolyte with different concentrations of inhibitors (from 20 ppm to 200 ppm by weight) dissolved in it. The electrochemical studies were carried out with N80 steel strips having an exposed area of 1 cm². The rest of the samples were isolated from the working environment by a cold mounting process, for which epoxy resin had been used. A conventional three-electrode cell consisting of N80 steel as a working electrode, platinum as counter electrode, and a saturated calomel electrode as reference electrode was used. Polarisation studies were carried out using an AMEL Potentiostat 2053, Italy, connected to a personal computer. Prior to electrochemical measurements, the working electrode was first immersed into the test solution for 30 min to establish a steady-state open circuit potential. After the establishment of the open circuit potential, dynamic polarization curves were obtained with a scan rate of 1 mV/s in the potential range from −470 to −390 mV with scan rate of 10 m Vs⁻¹. All potentials were measured against SCE. All experiments were performed at 30 ± 0.2°C in an electronically controlled air thermostat. The inhibition efficiency (IE %) was calculated using the following equation: where = corrosion current in the absence of inhibitor and = corrosion current in the presence of inhibitor.

AC-impedance studies were carried out in three-electrode cell assembly containing N80 steel as the working electrode, platinum as counter electrode, and saturated calomel as reference electrode. The impedance measurements were carried out at an open circuit potential (OCP), after 30 min immersion of the N80 steel electrode in the corrosive medium. The impedance data were acquired in the frequency range of 100 KHz–50 mHz with an AC voltage amplitude of 10 mV. The charge transfer resistance () and double-layer capacitance () were determined from Nyquist plots. The inhibition efficiencies were calculated from charge transfer resistance values by using the following formula: where = charge transfer resistance in absence of inhibitor; = charge transfer resistance in presence of inhibitor.

2.2.3. Scanning Electron Microscopic (SEM) Analysis

The N80 specimens of size 1.0 cm × 1.0 cm × 0.06 cm were abraded with a series of emery papers (grades 320, 500, 800, and 1200) and then washed with distilled water and acetone. After immersion in 15% HCl in the absence and the presence of optimum concentration of inhibitor (AMPT) at 30°C for 6 h, the specimen was cleaned with distilled water, dried with a cold air blaster, and then the SEM images were recorded using JEOL JSM-6380 LA analytical scanning electron microscope.

2.2.4. FT-IR Spectroscopy

For the FTIR studies the N80 steel coupons were immersed in 15% HCl containing optimum concentration of inhibitors (AMPT, APT, and ACPT) for 24 h. The test coupons were then removed from the solution, washed thoroughly with distilled water and dried. The film formed on the N80 surface in the presence of the inhibitor was collected by nonmetallic scrapper from the surface of the steel for spectral analysis with Fourier transform infrared spectroscopy (FT-IR). FT-IR spectra were recorded between 4000 cm⁻¹ and 400 cm⁻¹, and the scraped films were recorded using a Perkin Elmer Model 2000, by KBr pellet method.

3. Results and Discussion

3.1. Weight Loss Measurement

Corrosion inhibition efficiency (IE%) offered by inhibitors (AMPT, APT, and ACPT) has been evaluated by weight loss technique after 6 h of immersion at 303 K which is given in Table 3. From this table it is apparent that inhibition efficiency (IE%) was increased with the increase in the concentration of the inhibitor [23]. The maximum of 82.3% inhibition efficiency was obtained at the 200 ppm inhibitor (AMPT) concentration. No considerable effect on the inhibition efficiency (IE%) was observed by a further increase in the inhibitor concentration in the acid solution. From this table, the order of the inhibition efficiency follows the order AMPT > APT > ACPT. Corrosion inhibition studies were also carried out at different temperatures. Corrosion parameters, namely, corrosion rate (CR), surface coverage (), and inhibition efficiency (IE %) of N80 steel in 15% HCl in the presence and absence of inhibitor at different temperature, obtained from weight loss measurements, are shown in Table 4. As shown from this table, by increasing the concentration of the inhibitor, corrosion rate decreases; as a result, the inhibition efficiency was increased with rise in temperature [24]. For all concentrations of AMPT, the systems at 333 K gave the highest efficiencies. The maximum efficiency of 92% was obtained for 200 ppm AMPT at 333 K. The variation in corrosion rate with different concentration of thiadiazole derivatives in 15% HCl at different temperature is shown in Figure 1. It is evident from Figure 1 that the inhibitor (AMPT, APT, and ACPT) has shown remarkable corrosion inhibition at a higher temperature. The variation of inhibition efficiency with the temperature is shown in Figure 2. From this figure, order of the inhibition efficiency of thiadiazole derivatives is as follows: AMPT > APT > ACPT. High efficiency of these compounds was attributed to the presence of extensively delocalized electrons of the phenyl rings, planarity, and the presence of lone pair of electrons on N and S atoms which favored a greater adsorption of inhibitors on the metal surface [25].

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3.1.1. Thermodynamic and Activation Parameters

Thermodynamic and activation parameters play important role in understanding the inhibitive mechanism. The weight loss measurements were done in the temperature range of 303–333 K in the absence and the presence of different concentrations of inhibitors (AMPT, APT, and ACPT) in 15% HCl for N80 steel. The apparent activation energy () for dissolution of N80 steel in 15% HCl can be expressed using the Arrhenius equation, where CR is the corrosion rate, is the apparent activation energy, is the molar gas constant (8.314 J K⁻¹ mol⁻¹), is the absolute temperature, and is the Arrhenius pre-exponential factor. Figure 3 represents the Arrhenius plot of against 1/ for the corrosion of N80 steel in 15% HCl solution with or without the presence of AMPT, APT, and ACPT at concentrations ranging from 20 ppm to 200 ppm. From Figure 3, the slope of each individual line was determined, and the activation energy has been calculated by using ( = (slope) × 2.303 × ) and the values of were summarized in Table 5. It is evident from Table 5 that the decrease in activation energy indicates the retardation in corrosion rate which could have occurred because of the adsorption of the inhibitors at the surface of the metal [26].

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(b)

(c)

The value of enthalpy of activation of the and the entropy of activation can be calculated by using the following formula: where CR is the corrosion rate, is the enthalpy of activation, is the entropy of activation, is Planck’s constant, and is the Avogadro number, respectively.

A plot of log (CR/) against 1/(Figure 4) gave straight lines with slope of and intercept of () from which the activation thermodynamic parameters ( and ) are estimated and listed in Table 5. The results which are presented in Table 5 show that the enthalpy of activation is all positive. The positive sign of the enthalpy reflects the endothermic nature of the N80 steel dissolution process [27]. The negative value of (Table 5) for all the three inhibitors indicates that activated complex in the rate determining step represents an association rather than a dissociation step, meaning that a decrease in disorder takes place during the course of transition from the reactant to the activated complex, and the positive value of refers to an increase in the disorder [28].

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3.2. Potentiodynamic Polarization Measurements

The anodic and cathodic polarisation curves for the corrosion of N80 steel in 15% HCl in the presence and the absence of varying concentrations of inhibitors (AMPT, APT, and ACPT) at 303 K are shown in Figure 6. The linear Tafel segments of the cathodic and anodic curves were extrapolated to the point of intersection to obtain the corrosion potential () and corrosion current density (). The electrochemical parameters such as corrosion potential (), corrosion current density (), anodic () and cathodic () Tafel slope, and percentage inhibition efficiency (IE%) determined from polarisation curve are summarized in Table 6. The data in Table 6 clearly show that the current density decreases with the presence of thiadiazole inhibitors (AMPT, APT, and ACPT); this indicated that inhibitors adsorbed on the metal surface, and hence the inhibition efficiency increases with the increase in the inhibitor concentration up to an optimum value. Thereafter, the increase in the inhibitor concentration resulted in negligible increase in inhibition efficiency and the presence of inhibitor caused small changes in () value. This implies that the inhibitor acts as a mixed-type inhibitor, affecting both anodic and cathodic reactions [29]. According to Li et al. [30], if the displacement in is more than ±85 mV/SCE relating to (corrosion potential of the blank), the inhibitor can be considered as a cathodic or anodic type. If the change in is less than 85 mV, the corrosion inhibitor may be regarded as a mixed type. But the maximum displacement in the present case is less than 20 mV/SCE, which indicates that AMPT, APT, and ACPT act as mixed-type inhibitors. It is concluded that the inhibitor’s molecules retard the corrosion process without changing the mechanism of corrosion process in the medium of investigation. However, the shift of values towards positive direction on increasing the concentration of thiadiazole derivatives suggests anodic control over the reaction.

3.3. Electrochemical Impedance Spectroscopy (EIS)

Nyquist plots of N80 steel in 15% HCl solution in the absence and the presence of different concentrations of AMPT, APT, and ACPT at 303 K are shown in Figures 7(a), 7(b), and 7(c). It follows from Figures 7(a), 7(b), and 7(c) that a high frequency (HF) depressed charge-transfer semicircle was observed. The experimental data obtained from these plots are fitted by the equivalent electrical circuit shown in Figure 8. Such an equivalent circuit was also discussed by several researchers, who obtained similar depressed semicircles with single time constant due to surface heterogeneity of corrosion product covering the surface at random sites [31–33]. The charge-transfer resistance () values were calculated from the difference in impedance at low and high frequencies. The values of electrochemical double-layer capacitance () were calculated at the frequency , at which the imaginary component of the impedance is maximal by the following equation:

The constant phase element of double-layer (CPE) is mathematically expressed as where is a proportionality factor and “” has the meaning of phase shift. The value of “” represents the deviation from the ideal behavior and it lies between 0 and 1.

The charge transfer resistance (), double-layer capacitance () obtained from the Nyquist plots, and the calculated inhibition efficiency values (IE%) are shown in Table 7. It is clear that the value of increases with increasing the concentration of the inhibitor, indicating that the corrosion rate decreases in the presence of the inhibitor [34]. It is also clear that the value of decreases on the addition of inhibitors, indicating a decrease in the local dielectric constant and/or an increase in the thickness of the electrical double layer, suggesting that the inhibitor molecules function by the formation of the protective layer at the metal surface [35]. So, the changes in and values were caused by the steady replacement of the water molecules by the adsorption of inhibitor on mild steel surface, reducing the extent of dissolution [36]. The maximum inhibition efficiency was obtained for AMPT at 200 ppm concentration. Both electrochemical methods (polarization measurement and EIS study) offered nearly the same trend.

3.4. Adsorption Isotherm

Basic information on the interaction between the organic inhibitors and the N80 steel surface is obtained from various isotherms. Adsorption of these organic inhibitors has displaced the water molecule from the metal surface. The most commonly used adsorption isotherms are Langmuir, Temkin, and Frumkin. By far, the best fit was obtained with the Langmuir adsorption isotherm. The degree of surface coverage () for different concentrations of inhibitor in 15% hydrochloric acid has been evaluated by the weight loss value. According to the Langmuir adsorption isotherm, the surface coverage () is related to the inhibition concentration by the following equation: where is the inhibitor concentration and is the equilibrium constant for adsorption-desorption process.

A plot of (/) versus (Figure 5) gives a straight line with an average correlation coefficient (), (, 0.997, and 0.999) for AMPT, APT, and ACPT, respectively, at 303 K which suggests that the adsorption obeys Langmuir adsorption isotherm. From the intercept, is calculated, and by using the value of the value of was calculate by the following equation: where is the gas constant and is the absolute temperature (K). The value of 55.5 is the molar concentration of water in solution in mol L⁻¹. In the present study a large value of was found for all the three studied inhibitors indicating the strong adsorption of inhibitor molecules at the surface of N80 steel. The values of were −37.5, −35.2, and −32.1 kJ/mol for AMPT, APT, and ACPT, respectively. The negative values of indicate a spontaneous adsorption process and stability of the adsorbed film of (AMPT, APT, and ACPT) on N80 surface [37]. It is generally accepted that for the values of up to −20 kJ/mol, the types of adsorption were regarded as physisorption; the inhibition acts due to the electrostatic interactions between the charged molecules and the charged metallic surfaces, while the values around −40 kJ/mol or smaller were seen as chemisorption, which is due to the charge sharing or a transfer from the inhibitor’s molecules to the metal surface to form a covalent bond [38, 39]. The values of in our measurements range from −30 to −40 kJmol⁻¹; it is suggested that the adsorption of these molecules involves chemisorption.

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The inhibition efficiency afforded by all the three inhibitors may be attributed to the presence of electron rich (N, S) atoms and delocalized electrons. The possible coordinating centres are unshared electron pair of nitrogen of –NH₂ group, nitrogen of thiadiazole ring, C=N group, and -electrons of phenyl and thiadiazole rings. The participation of phenyl ring during the adsorption of the inhibitors may be shown by higher % IE value in case of methoxy substituents having +I effect and lower values for chlorosubstituent with −I effect.

3.5. Scanning Electron Microscopy (SEM)

The surface morphology of mild steel specimens exposed to 15% HCl solutions in the absence and presence of 200 ppm of AMPT are shown in Figures 9(a), 9(b), and 9(c). Figure 9(a) shows SEM image of polished bare N80 steel surface. Figure 9(b) reveals that the surface is severely corroded, and there is formation of different forms of corrosion products (iron oxides) on the surface in the absence of the inhibitor, and the entire surface is covered by a scale-like black corrosion product. The morphological feature of the inhibited surface with the addition of 200 ppm of AMPT is shown in Figure 9(c). On comparing these micrographs, it appears, that in the presence of inhibitors, the surface of the test material has improved remarkably with respect to its smoothness. The smoothening of the surface would have been caused by the adsorption of inhibitor molecules on it. But the closer look at such sites reveals that the inhomogeneities are due to the structural defects of the metal substrate and that these sites are also covered by the inhibitor film. This observation also accounts for the high inhibition efficiency values obtained during the weight loss studies of the inhibitor system.

3.6. FTIR Spectroscopic Analysis of Corrosion Product

The FTIR spectra of pure inhibitors and the surface films formed on N80 steel coupons immersed in 15% HCl containing optimum concentration of inhibitors (AMPT, APT, and ACPT) for 6 h are presented in Figures 10(a), 10(b), and 10(c). The FTIR spectra of pure AMPT show band at 3290 cm⁻¹, 3135 cm⁻¹, APT at 3355, 3160 cm⁻¹ and ACPT at 3280, 3120 cm⁻¹, which indicate the asymmetrical and symmetrical N–H stretching vibrations for the amino group. Bands at 3280 cm⁻¹, 3125 cm⁻¹ for AMPT, 3345, 3148 cm⁻¹ for APT, and 3272, 3113 cm⁻¹ for ACPT, respectively indicate the asymmetrical and symmetrical N–H stretching vibration for amino group. Strong peaks observed at 1640, 1630, and 1635 cm⁻¹ are attributed to the N–H in plane bending vibrations of the amino group in pure AMPT, APT, and ACPT, respectively. Strong peaks observed at 1626, 1622, and 1620 cm⁻¹ are attributed to the N–H in plane bending vibrations of the amino group in AMPT, APT, and ACPT, respectively. Strong bands at 1530, 1520, and 1525 cm⁻¹ are attributed to the stretching vibration of the C=N group in the ring in pure AMPT, APT, and ACPT, respectively. Strong bands at 1523, 1512, and 1514 cm⁻¹ are attributed to the stretching vibration of the C=N group in the ring in surface product of AMPT, APT, ACPT respectively. Peaks observed at 695, 690, and 680 cm⁻¹ are attributed to the ring C–S vibration for pur AMPT, APT, and ACPT, respectively. Peaks observed at 690, 684, and 670 cm⁻¹ are attributed to the ring C–S vibration for surface product of AMPT, APT, ACPT respectively. The presence of all the functional groups present in pure AMPT, APT, and ACPT in the spectrum of the surface product with a negative shift indicates the adsorption of inhibitors AMPT, APT, and ACPT at the surface of N80 steel.

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4. Conclusions

(1)The synthesized thiadiazoles show good inhibition efficiencies for the corrosion of N80 steel in 15 wt% HCl solutions and the inhibition efficiency increases with increasing the concentration of these inhibitors and with the temperature. The increasing order of inhibiting performance of the inhibitors is in the order of: AMPT > APT > ACPT.(2)Thiadiazoles inhibitors were found to be mixed-type inhibitors from Tafel polarization measurements. While one equivalent structure model was selected to fit the experimental data of the impedance diagram (EIS). And the results are good in agreement with weight loss measurements.(3)It is suggested from the results obtained from Langmuir adsorption isotherm that the mechanism of corrosion inhibition is occurring mainly through adsorption process.(4)Surface morphological studies such as FTIR and SEM analysis showed that a film of inhibitor is formed on the electrode surface.

Acknowledgment

One of the authors, Sumit Kumar, gratefully acknowledges Council for Scientific and Industrial Research (CSIR), New Delhi India, for research fellowship.

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Copyright © 2013 M. Yadav 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.

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