International Journal of Corrosion
Volume 2015 (2015), Article ID 548031, 12 pages
http://dx.doi.org/10.1155/2015/548031

Research Article

An Investigation of a Combined Thiourea and Hexamethylenetetramine as Inhibitors for Corrosion of N80 in 15% HCl Solution: Electrochemical Experiments and Quantum Chemical Calculation

Jun Hu,1,2 Yun Wang,¹ Lijun Yu,¹ Yongqiang Zou,¹ and Yuqi Wang1,2

¹School of Chemical Engineering, Northwest University, No. 229 North Road of Taibai, Xi’an, Shaanxi 710069, China
²Chemical Engineering Research Center of the Ministry of Education for Advanced Use Technology of Shanbei Energy, Xi’an, Shaanxi 710069, China

Received 5 March 2015; Accepted 28 April 2015

Academic Editor: Ksenija Babic

Copyright © 2015 Jun Hu 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.

The inhibition mechanism of thiourea (TU) and hexamethylenetetramine (HMTA) mixed in 15% HCl solution on N80 surface was investigated by potentiodynamic polarization, electrochemical impedance spectroscopy measurements, and surface morphology analysis. Quantum chemical calculations and molecular dynamics simulations were performed to study the properties of TU and HMTA. The results showed that the inhibitors can form strong bonds and stable films on the surface, which inhibits the cathodic and anodic reactions in HCl solution and reduces the diffusion coefficients of corrosive particles.

1. Introduction

Fracturing technique is one of the main measures to increase oil production. Acidic solution is commonly used as fracturing fluid, which can decompose the big molecules into small molecules in order to discharge the oil from the crack [1, 2]. However, acidic solution will make N80 carbon steel, the most used material in oil well, meet with corrosion easily [3].

The use of inhibitors is one of the most cost-effective and practical methods to protect metallic materials against corrosion in acidic medium [4, 5]. Organic compounds, which generally contain N, O, P, or S heteroatoms, are commonly used to control the corrosion damage of N80 [6–8]. Until now, there are a host of inhibitors that have been developed for N80, including acetylenic alcohols, aromatic aldehydes, alkenyl phenones, amines, amides, nitrogen containing heterocycles, nitriles, iminium salts, triazoles, pyridine and its derivatives or salts, quinoline derivatives, thiourea derivatives, thiosemicarbazide, thiocyanates, quaternary salts, and condensation products of carbonyls and amines [9, 10]. Among these inhibitors, thiourea (TU) and its derivatives have aroused widespread concern due to its adsorption on various metal surfaces [11, 12]. A few studies investigated its potential use as an inhibitor for metal corrosion because their results manifested that the single TU molecule films contained a lot of defects. The stable adsorption layers of single TU molecules could only be formed on the surface of weakly negatively and positively charged electrodes [13–15]. Therefore, it might be a better choice to improve the inhibition efficiency by mixing another inhibitor to the solution at a proper proportion and overcome the disadvantages of a single inhibitor [16]. Recently, some studies focused on obtaining inhibitors with high inhibition efficiency in this way [17–19]. Hexamethylenetetramine (HMTA), which can also form a single molecular layer on metal surfaces by adsorption, is another shared inhibitor used in acidic environments [20]. So far, a few studies had been published on the inhibition effects of a solution containing a mixture of TU and HMTA.

The objective of this paper is to investigate the inhibition action of TU and HMTA on surface of N80 steel in acidic medium by potentiodynamic polarization measurements, electrochemical impedance spectroscopy (EIS) measurements, and surface analysis and through structure analyses using quantum chemical simulation.

2. Materials and Methods

2.1. Materials

N80 carbon steel specimens were used with chemical composition (wt.%): 0.42% C, 0.24% Si, 1.55% Mn, 0.012% P, 0.004% S, 0.051% Cr, 0.18% Mo, 0.005% Ni, 0.01% Ti, 0.06% Cu, and Fe balance. The chemical structures and names of TU and HMTA are shown in Table 1. All specimens were manually mirror-polished by using grit SiC polishing papers with the grit size of 400, 800, and 1000, respectively. Thereafter, they were immersed in petroleum ether for 10 minutes, then washed thoroughly with bidistilled water, degreased with acetone, washed again with bidistilled water, and finally dried at room temperature.

Table 1: Chemical structures and names of the studied thiourea and hexamethylenetetramine.

Structure
Name and abbreviation

Thiourea (TU)

Hexamethylenetetramine (HMTA)

For electrochemical measurements, specimens were cut into circular column with a dimension of Ф14.5 mm × 5 mm by using wire cutting method. Then, specimens were put into the sample support made by Teflon and only an active surface area of 10.5 mm was exposed to the solution for electrochemical measurement. The electrode was immersed for 24 h to retain stable before starting the measurements. The experiments were conducted in oxygen-free environment. The experimental temperatures were controlled at 25 ± 1°C by a thermostat water bath during all experiments. The electrolyte solution was made from HCl and bidistilled water. The inhibitors were obtained from Sigma-Aldrich (USA) and used without any pretreatment.

2.2. Solution Preparation

The corrosion solution of 15% HCl was prepared from 37% HCl using distilled water. The concentration range of TU varied from 4.0 × 10⁻⁶ to 4.0 × 10⁻³, and the concentration of HMTA was from 0.0001 to 0.1.

2.3. Surface Analysis

Scanning electron microscope (SEM) studies and energy dispersive X-ray analysis (EDX) were performed to observe the morphology and discuss quantitative analysis of elements on the surface morphologies of N80 steel samples using VEGA3 TESCAN after immersions for 24 h in the absence and presence of optimum concentration of the inhibitor at 25 ± 1°C. The energy of the acceleration beam employed was 20 kV.

2.4. Electrochemical Measurements

The corrosion rate on the surface of N80 was evaluated by electrochemical measures in 15% HCl at 25°C. A conventional three-electrode system was used in all electrochemical measurements, which includes a working electrode, a saturated calomel electrode and platinum electrode. The electrochemical experiments were carried out with external potential. Electrochemical impedance spectroscopy (EIS) was performed at open circuit potential in the frequency range from 10 mHz to 100 kHz by superimposing alternating current signal of 10 mV after immersion for 24 h in the corrosive solution. The polarization curves were recorded from −250 mV to 250 mV (vs. SCE) with a scan rate of 0.1 mV s⁻¹. In order to confirm the stability of the corrosion environment and the reproducibility of the experiments, each experiment was repeated three times.

2.5. Theoretical Calculations

Quantum chemical calculations can provide insight into the design of inhibitor systems with superior properties and elucidate the adsorption process at a molecular level [21–26]. The Dmol³⁺ and Discover modules of the Materials Studio 7.0 software (Accelrys Inc.) were employed for the quantum chemical calculations. The first indispensable step was to build and optimize TU and HMTA molecules and a 3-dimensional Fe (1 1 1) surface (because the main elements of N80 is Fe). Afterwards, a COMPASS force field was distributed on the structure. Then, the Amorphous Cell module was used to build the amorphous structure containing 100 molecules of corrosion inhibitors and 5 chloride ions and oxygen molecules. At last, the optimized Fe surface and the corrosion inhibitors were used to simulate 167.2 nm × 167.2 nm × 362.4 nm oxide film/corrosion inhibitor solution/vacuum layer structures.

During simulation, the position of the Fe atoms was fixed and the corrosive medium particles were modelled with the Discover module assuming a canonical ensemble (NVT) to simulate the diffusion through the corrosion inhibitor film. The simulation temperature was set at 25°C and both temperature and pressure were controlled by the Andersen-Berendsen method. The distribution of the starting speed of the molecules was described by a Maxwell-Boltzmann distribution, assuming periodic boundary conditions and the equivalence of the time average and the ensemble average, for example, by using the Velocity Verlet algorithm to integrate Newton’s equation of motion. Van der Waals and Coulomb interactions were simulated by using the charge group method. A truncation radius of 1.5 nm was selected (spline width: 0.10 nm, buffer width: 0.05 nm), and the truncation distance was corrected for intermolecular interactions according to the average density approximation method. A simulation time of 5000 fs was chosen with a step length of 1.0 fs. The trajectory of a frame was recorded every 50 steps, resulting in a total output of 100 frames.

3. Results and Discussion

3.1. Surface Morphology Analysis

Scanning electron microscope (SEM) and energy dispersive X-ray analysis (EDX) images were obtained in order to analyze the surface morphology of the blank material of N80, in the absence and presence of inhibitor after 24 h at 25 ± 1°C. Figure 1(a) manifests N80 sample that was not exposed to 15% HCl solution, observing a smooth surface. Figure 1(c) reveals that the N80 surface exposed to 15% HCl solution is damaged uniformly in the absence of inhibitors. Figure 1(e) shows surface in 15% HCl solution with 0.004 M TU and 0.1 M HMTA, showing a protective layer. This is because of the formation of an adsorbed film of TU and HMTA preventing corrosion of N80 in 15% HCl solution.

Figure 1: SEM image and EDS analysis of the N80 before exposure to 15% HCl medium (a) and (b) after exposure to the acidic medium (c) and (d), in 15% HCl medium with the addition of 0.004 M TU and 0.1 M HMTA (e) and (f) at 25 ± 1°C, respectively.

Energy dispersive X-ray (EDX) was carried out in order to analyze surface composition of the formed protective film. In Figure 1(b), two signals of Fe element can be observed, showing the main constituent element of N80. The characteristics peak of Fe, Cl and small characterizing peak of O are detected in hydrochloric acid solution (Figure 1(d)). The weight percentage of Cl is up to 30.30% based on EDX data; it revealed that the oxide film on the surface of N80 was damaged by chloride in corrosive medium; Fe surface is dissolved and formed FeCl₂; thus, these peaks represent the corrosion products formed on the surface. When TU and HMTA were added into hydrochloric acid medium (Figure 1(f)), the peaks of Fe become small in comparison to the samples without inhibitor molecule; at the same time, the intensity of Cl and O peaks are also dropped. The decrease of the Fe, Cl, and O peaks and also the appearance of C peak are indicative of the formation of adsorptive inhibitor film on the surface of N80. Consequently, the organic corrosion inhibitor film increases the transfer resistance of chloride ions from solution to metal surface and slows down the corrosion triggered by chloride ions.

3.2. Electrochemical Experiments

3.2.1. Potentiodynamic Polarization Measurements

The anodic and cathodic polarization curves for N80 measured after 24 h of immersion in 15% HCl solution containing varying concentrations of TU and HMTA at 25 ± 1°C are shown in Figure 2.

Figure 2: Anodic and cathodic polarization curves for N80 in 15% HCl in the absence and presence of various concentrations of TU and HMTA derivatives at 25 ± 1°C.

As it is seen in Figure 2, a lower current density was observed for cathodic curves in the presence of TU and HMTA in HCl solution. However, the anodic curves are nearly the same, thus pronouncing more cathodic reaction.

For the cathodic polarization curve, the versus is almost linear. In this case, the strong electric field intensity provides sufficient driving force for the diffusion of H⁺ ions from the solution to the film. Furthermore, the diffusion of oxygen also exists. Therefore, the cathodic corrosion reaction in 15% HCl solution is described by the following reaction (1):

Adding the inhibitors strongly reduces the cathodic corrosion density compared to the pure HCl solution, indicating that the inhibitor can decrease the speed of reaction (1). Due to the adsorption of the inhibitor on the N80 surface, the active sites are covered, and the adsorbed inhibitor film will induce an extra energy barrier for the diffusion of H⁺. Furthermore, the film can also reduce the diffusion of oxygen. In summary, these factors restrain the cathodic corrosion process.

Anodic polarization lines show the dissolution of Fe into Fe²⁺ and proceed in the form of corrosion [27] and the diffusion of Fe²⁺ from the outer Helmholtz plane into the bulk solution [28]. After adding the inhibitors, the slopes of the anodic polarization lines nearly unchanged, indicating that the presence of the inhibitors in the solution has little effect on the dissolution rate of N80.

The corresponding corrosion potential (), corrosion current density (), anodic Tafel slopes (), and cathodic Tafel slopes () are listed in Table 2, and the values were calculated using (2)–(4). Subsequently, the inhibition effects were then calculated using (5). One can see the following:

Table 2: Corrosion kinetics parameters of N80 in 15% HCl solution with different corrosion inhibitor.

Sample (M)
(mV)
(mV)
(V)
(A·cm⁻²)
(%)

15% HCl
118.37
146.65
−0.519
6.467
—

0.1 M TU
95.52
124.73
−0.519
0.351
94.57

4.0 × 10⁻³ M HMTA
110.89
131.9
−0.503
0.322
95.02

15% + 4.0 × 10⁻⁵ M TU + 0.001 M HMTA
81.04
103.49
−0.559
0.637
90.14

15% + 4.0 × 10⁻⁴ M TU + 0.01 M HMTA
77.38
111.06
−0.548
0.419
93.52

15% + 4.0 × 10⁻³ M TU + 0.1 M HMTA
82.62
88.85
−0.584
0.287
95.56

Table 2 shows that the values of and for the pure HCl solution are extremely larger than other cases, indicating that passive films were formed on the N80 surface after adding the inhibitors. After adding the inhibitors, the values for and did not significantly change, which means that the anodic and cathodic reactions were similar.

The corrosion current density is one of the most crucial indicators for the evaluation of the corrosion resistance. The corrosion current density () on the N80 electrode in 15% HCl solution in the absence of inhibitor is 6.467 × 10⁻³ A·cm⁻², and the corrosion potential is −0.519 V(SCE). In general, the corresponding corrosion potential is decreased after adding inhibitors; this mainly attributes to the restrain of cathodic reactions. The corrosion current densities decrease with the increasing inhibitor concentration. The lowest dissolution current density on the N80 occurs at the highest inhibitor concentration. From Table 2, when the TU was added into HCl solution, the value of is lower than that in HCl solution obviously. Thus, the efficiency calculated by (5) is 94.57%. It indicates that TU was adsorbed in the active site of the electrode surface, and the rate of corrosion on the surface of N80 decreased. In addition, HMTA also has a high efficiency for N80 in HCl solution by the results. When the TU and HMTA were added to HCl solution, the higher the concentration of TU and HMTA is, the lower the value of is. The corrosion potential shifts to negative direction. The value of is 0.287 × 10⁻³ A·cm⁻² in a solution containing 0.004 M TU and 0.1 M HMTA, which is smaller compared with the inhibitors alone. This suggests that adding TU and HMTA have synergistic effect. The highest observed inhibition efficiency was 95.56%, the decrease in the current density is attributed to the adsorption of the inhibitor molecules on the N80 surface, forming a protective layer and blocking the active sites on the metal surface.

3.2.2. Electrochemical Impedance Spectroscopy (EIS) Measurements

To get further information concerning the inhibition process, EIS measurements on the N80 electrode were performed. EIS is capable of in situ and nondestructively probing relaxation phenomenon over a wide frequency range [29]. Nyquist and Bode plots of N80 electrode in 15% HCl are shown in Figure 3.

(a)

(b)

Figure 3: Electrochemical impedance spectroscopy diagrams for N80 electrode in 15% HCl solution in the absence and presence of various concentrations of a mix of both inhibitors, TU and HMTA, at 25 ± 1°C: (a) Nyquist plots, (b) Bode plots.

The Nyquist plots obtained for N80 in 15% HCl in the absence and presence of various concentrations of the TU and HMTA are shown in Figure 3(a). These plots were characterized by a semicircular capacitive loop at high frequency. The Nyquist plot contains a capacitive loop in high frequency region, the center of capacitive loop lies under the real axis, which is related to the roughness, inhomogeneity of the solid surfaces, or adsorption of inhibitors. It is worth noting that the high frequency region should mainly display quick responses of the inhibitor film [30, 31]. The capacitive loop is linked to the charge transfer resistance of the inhibitor film. Figure 3(a) shows that the capacitive loops become stronger with an increase of the inhibitor concentration, mainly due to the absorption of the inhibitor at the active sites on the N80 surface and the formation of a continuous film, exhibiting a barrier effect. It would effectively protect the metal from aggressive attack by the solution, which increases the charge transfer resistance.

The plot in the medium frequency range is an oblique line, indicating that the system has a predominant capacitive behaviour. For frequencies higher than 10³ Hz, the values of in the solutions containing inhibitors are about 1–3 Ω·cm⁻² except the experiment that contains 0.004 M TU and 0.1 M HMTA. This shows that only the resistance of the solution was detected in this region. It might show some rearrangements or a partial desorption of the inhibitor. In 0.004 M TU and 0.1 M HMTA, the values of gradually increase from 2 Ω·cm⁻² to 33 Ω·cm⁻², indicating that there are strong interactions between metal surface and inhibitor and the desorption process is arduous to occur.

The equivalent circuit, shown in Figure 4, was used to fit the EIS data.

Figure 4: The equivalent circuit used to model the electrochemical impedance spectroscopy data at open circuit potential at 25 ± 1°C.

In the equivalent circuit, is the solution resistance; is the charge transfer resistance; and denote the constant phase elements representing the capacitance of the electric double layer and inhibitor film, respectively; and denotes the resistance of inhibitor film [32]. Table 3 lists the fitting parameters obtained by using corresponding equivalent circuits.

Table 3: Electrochemical parameters calculated from EIS measurements on N80 electrode in 15% HCl solution for different corrosion inhibitor concentrations at 25 ± 1°C.

Sample (M)
(Ω cm²)
(S  cm⁻²)
()
(Ω cm²)
(S  cm⁻²)
()
(Ω cm²)

HCl
0.9203
0.0002918
0.9054
32.25
0.0003987
0.8785
3.943

0.0001
5.235
0.0004901
0.8346
11.29
0.0001136
1
59.84
0.934

0.001
1.175
0.0000483
0.929
239.5
0.0005603
0.9017
123.3
0.968

0.01
1.307
0.0003884
0.9332
94.47
0.0000725
0.9408
143.6
0.973

0.1
1.884
0.0003417
0.9068
136.4
0.00004803
0.9515
210.4
0.981

According to Table 3, the changes of are small. Based on the definition of the capacitance, the changes of can be mainly attributed to (the relative dielectric constant) and the thickness of the film. In the pure HCl solution, the value of is similar to the value of the dielectric constant for water. After adding the inhibitors, the value of is equal to the value of the dielectric constant for the inhibitors due to the absorption of the inhibitors on the N80 surface; thus, will decrease after adsorption. At the same time, the thickness of the film will increase due to adsorption of the inhibitors on the N80 surface. The combination of these factors is leading to a decrease of . Because is related to the roughness and the heterogeneity of the surface, stands for an ideal capacitance [33], and the values of also verify these results. The increases gradually along with the concentration of inhibitors, which indicates that the film became integrated gradually. The increase of is suggestive of the increase of charge transfer resistance of the inhibitor film gradually, which is attributed to the formation of protective film on the metal/solution interface.

Kramers-Kronig (K-K) transformation is often used as an independent check for the validity of the impedance data. Most frequently, when applied to EIS data, the transformation equations are written as follows [34]:

where is the transformation frequency, is the integration frequency, and and denote the real and imaginary components of the impedance, respectively. Equations (1) and (2) provide the imaginary axis-to-real axis transformations, while (3) yields the real axis-to-imaginary axis transformation. The measurement and fitting error of the impedance are manifested in Figure 5 for five different etching solutions.

Figure 5: Measurement and fitting error of for N80 after exposure to four different solutions at open circuit potential and 25 ± 1°C.

The chi-square errors for each of the impedance spectroscopy data set are 2.29 × 10⁻³, 3.97 × 10⁻³, 2.11 × 10⁻³, 6.37 × 10⁻³, and 1.72 × 10⁻³, respectively, for the different solutions. As shown in Figure 5, the relative errors between the transformation data and the experimental data are in the range of 10% except at some points. Since some random errors of the system are inevitable to occur, the experimental data and the fitting result can be considered to be in perfect agreement. Therefore, the quintessential random distribution of the errors obtained in the fitting data indicates that the K-K transformations are consistent with the experimental data and the equivalent circuit is a suitable tool for the analysis.

3.3. Adsorption Isotherm

The surface coverage is a paramount parameter for the evaluation of the quality of the corrosion inhibitor film. The surface coverage can be used to calculate the following formula proposed by Shu et al. [35]:

where and are the charge transfer resistance for N80 in the absence and presence of the inhibitor, respectively. Based on the calculations, the highest obtained value for is 0.981.

The adsorption of organic molecules provides information concerning the interaction among the adsorbed molecules themselves as well as their interaction with the electrode surface [36]. The most frequently used adsorption isotherms are the Langmuir, Temkin, and Freundlich [37, 38]. The experimental data was fitted by using these adsorption isotherms and it was found that Langmuir absorption provided the best agreement with the experimental results. The Langmuir adsorption isotherm can be expressed as follows:

where is the constant of the adsorption equilibrium including the adsorption-free energy and is the inhibitor concentration [39]. The corresponding plot for the Langmuir adsorption isotherm is demonstrated in Figure 6.

Figure 6: Langmuir adsorption isotherm model for N80 in 15% HCl containing a mix of the inhibitors TU + HMTA at 25 ± 1°C.

The value of is related to the standard-free energy of adsorption, , calculated by as follows [40–42]:

where is the gas constant and is the absolute temperature.

In this case, the value of is −35.50 kJ·mol⁻¹, which suggests that the adsorption mechanism of TU and HMTA on N80 surface mainly involves chemisorption [43, 44]. At first, water molecules are adsorbed on the N80 surface and the adsorption of the inhibitors occurs due to electrostatic interaction, followed by the removal of water molecules from the surface. Afterwards, chemical interactions will occur between the metal surface and the inhibitors due to the short distance. Because chemisorptions yield more stable bonds than physisorption, the formed film is stable.

3.4. Quantum Chemical Calculations

The electronic parameters give the information concerning the interaction between inhibitor and metal surface. Quantum chemical calculations are the most used method to understand electronic distribution of a molecule [45–47]. Some properties of the inhibitors calculated by quantum chemical calculations are presented as shown in Figure 7.

Figure 7: The optimized structures and molecular orbital plots for inhibitors.

Figure 7 shows the optimized geometries and Mulliken atomic charges of TU and HMTA. Usually, the negative atomic charges are the adsorbed center because the electrons around the negative atomic can easily move to the unoccupied orbital of the metal/metal oxide. Figure 7 manifests that the most negative atomic charges happen in the N atomic for every inhibitor. The N atomic charges are −0.829 and −0.305 for TU and HMTA, respectively. This indicates that N is easily absorbed into N80 surface than other atoms. The map of the highest occupied molecular orbital (HOMO) and the lowest unoccupied molecular orbital (LUMO) also verify that the heterocyclic ring has high tendency to donate electrons to the metal surface. The quantitative results of quantum chemical parameters are calculated as shown in Table 4.

Table 4: Quantum chemical parameters derived for different inhibitors.

Inhibitors
Total energy
HOMO
LUMO

(kJ mol⁻¹)
(kJ mol⁻¹)
(kJ mol⁻¹)
(kJ mol⁻¹)
(debye)
(kJ mol⁻¹)
(kJ mol⁻¹)
(kJ mol⁻¹)

TU
1.47 × 10⁶
−483.6
−51.2
432.5
3.545
483.6
51.2
267.4
216.3
0.45

HMTA
−1.29 × 10⁶
−477.6
98.3
575.9
0.014
477.6
−98.3
189.7
287.9
0.47

According to the frontier molecular orbital theory of chemical reactivity by Fukui, most of the electron transition will happen at the frontier orbitals, named HOMO and LUMO of reacting species. The energy of HOMO () is directly related to the ionization potential and characterizes the susceptibility of the molecule toward attack by electrophiles; it is a measure of electron donating ability of inhibitors and explains the adsorption on N80 surfaces by a way of delocalized lone pair of electrons. The for HMTA is −477.6 kJ·mol⁻¹ and TU −483.6 kJ·mol⁻¹. This indicates the bond of HMTA formed on the surface of N80 is stronger than that of TU. The energy of LUMO (), which stands for the ability of electron receiving tendency, is directly related to the electron affinity and characterizes the susceptibility of the molecule toward attack by nucleophiles [48, 49]. The lower the values of are, the stronger the electron accepting abilities of the molecules are. The LUMO of N80 can accept the electron of inhibitors in the HOMO. Based on these parameters, the calculated difference () demonstrates inherent electron donating ability and measures the interaction of the inhibitor molecule with the N80 surface. The for TU and HMTA are 432.5 kJ·mol⁻¹ and 575.9 kJ·mol⁻¹, respectively. Because the molecules with small value have greater reactivity than molecules that have large value, it can be concluded that TU have more affinity on N80 surface.

The effect of dipole moment, , of inhibitor creates a significant static electric field that leads to upward/downward bending of surface energy. From Table 4, it can be seen that the dipole moment of TU is 3.545 debyes. So, there are polar molecules. It can be interpreted that TU will have interaction with other polar molecules in solution such as water and H⁺ molecule. Experimental results verify the simulated results [50]. For TU, it has great interaction with water in the solution. Accordingly, the TU film will have an ocean of defects.

Some other parameters such as , , and are also calculated. Based on Hartree-Fock theorem, the ionization potential () and the electron affinity () are given by

For absolute electronegativity, , and global hardness, , their operational and approximate definitions are as follows:

Two systems, N80 and inhibitor, are brought together, and electrons will flow from lower (inhibitor) to higher (N80), until the chemical potentials become equal. The fraction of electrons transfer, , will be given as follows [51, 52]:

In order to calculate the fraction of electrons transferred, a theoretical value for the absolute electronegativity of N80 according to Pearson was used  kJ·mol⁻¹ and a global hardness of , by assuming that the Fe atoms are softer than the neutral metallic atoms.

The global hardness, , is a parameter that gives paramount information concerning the reactive behavior of the molecule. The values of for TU and HMTA are 216.3 and 287.9 kJ·mol⁻¹, respectively. Therefore, the calculated reactivity order for the derivatives in aqueous phase inhibitors is TU > HMTA.

is the fraction of electrons transferred from inhibitor to the N80 surface. The values of manifested inhibition effect resulted from electrons donation. If , the inhibition efficiency would improve with increasing electron donating ability at the metal surface [53]. From Table 4, it can be concluded that TU and HMTA have greater ability of electrons donation to formed inhibitive adsorption layer.

3.5. Molecular Dynamics Analysis

The adsorption structures of TU and HMTA on N80 (1 1 1) surface were constructed using molecular dynamics simulation. The possibility of their adsorption on the N80 (1 1 1) surface was simulated as in Figure 8.

(a) TU

(b) HMTA

(c) TU + HMTA

Figure 8: Mode of adsorption of inhibitors on the Fe (1 1 1) surface at 25 ± 1°C: (a) TU, (b) HMTA, and (c) TU + HMTA.

Figure 8 shows the equilibrium configuration of the inhibitors. It can be seen that the adsorption occurred through the nitrogen atom for TU and the distance between surface and TU is long. For HMTA, there are no preferential directions for adsorption and the distance between surface and HMTA is small. For a combination of TU and HMTA, it can be seen that the adsorption of HMTA is not greatly changed. However, the TU molecules move closer to the N80 surface and the locations of adsorption on the N80 surface are changed into nitrogen and sulfur due to the interaction between TU and HMTA.

The corresponding interaction energies between the N80 surface and the inhibitor molecules were calculated and are listed in Table 5.

Table 5: Interaction and binding energy of the benzotriazole derivatives on N80 surface at 25 ± 1°C.

Inhibitors
/kJ mol⁻¹
/kJ mol⁻¹
/kJ mol⁻¹
Interaction energy/kJ mol⁻¹
Binding energy/kJ mol⁻¹

TU
7383.014504
7572.479812
−119.554346
−69.911
69.911

HMTA
6101.689515
6818.939516
−590.948316
−126.302
126.302

TU + HMTA
5441.742410
6012.418128
−438.324184
−132.352
132.352

The interaction energy is the key parameter to evaluate the inhibition performance. The interaction energies obtained are −69.911 kJ·mol⁻¹, −126.302 kJ·mol⁻¹, and −132.352 kJ·mol⁻¹ for different cases. It can be seen that the interaction energy between N80 (1 1 1) surface and TU is small, which is in agreement with the previous adsorption results. Furthermore, the combination of TU and HMTA will increase the interaction energy between N80 (1 1 1) surface and inhibitors.

Diffusion coefficients can be used to quantitatively describe the diffusion ability of corrosion medium particles in the corrosion inhibitor film. The smaller the corrosive medium particles of diffusion coefficient are, the better the performances of the corrosion inhibitor film are. The diffusion coefficient () of the corrosive particles can be obtained through the Einstein relation as follows:

is the number of diffusion atoms in the system, and represent the location of inhibitors molecule or particle in and initial time, and represents the curve slope of mean square displacement (MSD) to time. The diffusion coefficient can be obtained using (13) in the different corrosion inhibitors, as shown in Figures 9 and 10.

Figure 9: The diffusion coefficient () of oxygen in three inhibitors film at 25 ± 1°C.

Figure 10: The self-diffusion coefficient () in three inhibitors film at 25 ± 1°C.

It can be seen from Figure 9 that the diffusion coefficients of oxygen greatly decrease if both TU and HMTA are added to the solution and it can be concluded that a more stable film will form in this case, which has been also verified by previous cathodic polarization curves. Furthermore, Figure 10 indicates that the self-diffusion coefficients are 2.437 × 10⁻⁷ m²·s⁻¹, 8.496 × 10⁻⁷ m²·s⁻¹, and 1.145 × 10⁻⁸ m²·s⁻¹ for TU, HMTA, and the combination of TU and HMTA at 25 ± 1°C, respectively. It can be seen that the self-diffusion coefficients greatly decrease if both TU and HMTA are added to the solution and it can be concluded that a more stable film will form in this case.

3.6. Inhibition Mechanism

Generally, two types of inhibition mechanism were proposed. One was the formation of polymeric complexes with N80 ions depending on the applied conditions [54]. Another was forming a protective film on the N80 surface. Based on the above analysis, it can be determined that the inhibition mechanism of this inhibitor is the second one. The dynamic process of the formation of the protective film can be described as follows. When the inhibitors are added to the solution, the reactive metal surface will change to the passive state due to the adsorption of the inhibitor molecules on the surface. The adsorption can be described mainly by chemisorption, which will occur through the N and S of TU and HMTA due to its inherent electron donor ability.

TU has inherent electron donor ability to the metal surface due to the lower and values; it also strongly interacts with the water molecules in the solution. Because it is a polar molecule with , the interaction energy between metal surface and TU is only 69.911 kJ·mol⁻¹. The case is the opposite for HMTA. Although HMTA has a smaller inherent electron donor ability to the metal surface than TU, it has repulsive effects on the water molecules because it is a nonpolar molecule with . Combining the two of them not only enhances the films integrity, but also increases the resistance against diffusion of oxygen molecules from the solution to the N80 surface.

4. Conclusions

In this paper, the combined use of TU and HMTA as corrosion inhibitors for N80 surfaces in 15% HCl solution was systematically investigated by electrochemical experiments and quantum chemical calculations. The main conclusions can be summarized as follows.

(1)The results of SEM-EDX analysis manifested that the presence of inhibitors TU and HMTA in appropriate concentration was able to detect protective film on the surface of N80 samples and reduce the damage of chloride ions in comparison to the samples without inhibitors.(2)The combined use of TU and HMTA in 15% HCl solution yields an excellent corrosion inhibition effect, regarding cathodic reactions in a hydrochloric acid solution. The highest observed inhibition efficiency was 95.56%.(3)The adsorption of the mixture on the N80 surface can be described by the Langmuir isotherm, the highest surface coverage is 0.981, and the free energy of adsorption is −35.50 kJ·mol⁻¹. The inhibition mechanism of the inhibitors includes the formation of a protective film on the N80 surface mainly due to chemisorption. The protective film will reduce the diffusion coefficients of corrosive particles.

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

Acknowledgments

The financial supports from the National Natural Science Foundation of China (no. 51301132), Specialized Research Fund for the Doctoral Program of Higher Education (no. 20136101120009), Chinese Postdoctoral Science Foundation (2014M550507), and Shaanxi Technology Committee Industrial Public Relation Project (2014K08-28) are greatly acknowledged. This research project was supported by Central for High Performance Computing of Northwestern Polytechnical University, China.

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