Next Article in Journal
Investigation of High-Performance Electrode Materials: Processing and Storage Mechanism
Previous Article in Journal
Concrete Performance Produced Using Recycled Construction and By-Product Industrial Waste Coarse Aggregates
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

The Synergistic Inhibitions of Tungstate and Molybdate Anions on Pitting Corrosion Initiation for Q235 Carbon Steel in Chloride Solution

1
Key Laboratory of Coordination Chemistry of Jiangxi Province, College of Chemistry and Chemical Engineering, Jinggangshan University, Ji’an 343009, China
2
Guangxi Key Lab of Agricultural Resources Chemistry and Biotechnology, College of Chemistry and Food Science, Yulin Normal University, Yulin 537000, China
3
Key Laboratory of Green Chemical Process of Ministry of Education, School of Chemical Engineering and Pharmacy, Wuhan Institute of Technology, Wuhan 430205, China
*
Authors to whom correspondence should be addressed.
Submission received: 11 November 2022 / Revised: 2 December 2022 / Accepted: 12 December 2022 / Published: 16 December 2022

Abstract

:
In this work, the synergistic inhibitions of tungstate (WO42−) and molybdate (MoO42−) anions, including role and mechanism, on the initiation of pitting corrosion (PC) for Q235 carbon steel in chloride (Cl) solution were investigated with electrochemical and surface techniques. The pitting potential (Ep) of the Q235 carbon steel in WO42− + MoO42- + Cl solution was more positive than that in WO42− + Cl or MoO42− + Cl solution; at each Ep, both peak potential and affected region of active pitting sites in WO42− + MoO42− + Cl solution were smaller than those in WO42− + Cl or MoO42− + Cl solution. WO42− and MoO42− showed a synergistic role to inhibit the PC initiation of the Q235 carbon steel in Cl solution, whose mechanism was mainly attributed to the influences of two anions on passive film. Besides iron oxides and iron hydroxides, the passive film of the Q235 carbon steel formed in WO42− + Cl, MoO42− + Cl, or WO42− + MoO42− + Cl solution was also composed of FeWO4 plus Fe2(WO4)3, Fe2(MoO4)3, or Fe2(WO4)3 plus Fe2(MoO4)3, respectively. The film resistance and the defect quantity for Fe2(WO4)3 plus Fe2(MoO4)3 film were larger and smaller than those for FeWO4 plus Fe2(WO4)3 film and Fe2(MoO4)3 film, respectively; for the inhibition of PC initiation, Fe2(WO4)3 plus Fe2(MoO4)3 film provided better corrosion resistance to Q235 carbon steel than FeWO4 plus Fe2(WO4)3 film and Fe2(MoO4)3 film did.

1. Introduction

Pitting corrosion (PC) is one of the most common and universal localized forms of corrosion for metals and alloys, and the remarkable characteristic of PC is latent, random and sudden, particularly during the process of PC initiation [1]. Therefore, it is generally accepted that the key point of PC inhibition is restraining the nucleation of the corrosion pit [2].
It is confirmed that for metals and alloys working in service environments, there are two essential factors for the initiation of PC: the establishment of surface passivation on metals and alloys and the presence of aggressive anions in service environments, particularly the chloride anion (Cl) [1]. Further, it is reported repeatedly that in the service environments of metals and alloys, the addition of an introduced substance, mainly some inorganic and organic species, can inhibit the initiation of PC effectively [3]. At present, reported inorganic species for the inhibition of PC initiation include borate (BO43−) [4], tetraborate (B4O72−) [5], chromate (CrO42−) [6], dichromate (Cr2O72−) [7], molybdate (MoO42−) [8], nitrite (NO2) [9], nitrate (NO3) [6], phosphate (PO43−) [6], tripolyphosphate (P3O105−) [10], tungstate (WO42−) [11] anions and so on; by contrast, reported organic species for inhibiting PC initiation are relatively more, such as benzotriazole (BTA) [12], calcium lignosulfonate (CLS) [13], imidazoline (IM) [14], octaphenylpolyoxyethyiene (OP) [15], sodiumdodecylbenzenesulfonate (SDBS) [16], sodium dodecyl sulfate (SDS) [17], sodium oleate (SO) [18], thioureido imidazoline (TAI) [19], tetrabethylenepentamine (TEPA) [20], vitamin B5 [21] and others. However, in recent years, the research of PC inhibition has begun to focus on the synergistic role and mechanism of two or more species, and the conclusion that the simultaneous additions of some species into environmental media exhibit a better role for PC inhibition than the single addition of corresponding one species do has been proposed [22,23,24,25,26,27,28,29,30,31]. Up to now, confirmed combinations owning a synergistic role for PC inhibition are as follows: B2O72− and PO43− [22], Cr2O72− and MoO42− [23], MoO42− and NO2 [24], MoO42− and BTA [25], MoO42− and CLS [26], NO2 and TAI [27], NO2 and TEPA [28], WO42− and CLS [29], CLS and SO [30], IM and OP [31], and so on.
Carbon steel is a kind of metal engineering material with relatively weak surface passivation capability; therefore, in pure chloride solution, general corrosion is the main type of corrosion damage for carbon steel [2]. Further, for carbon steel in pure chloride solution, it is reported largely that the additions of organic species and their adsorption role as well as the additions of inorganic species and their film-forming role can inhibit the general corrosion of carbon steel [32]. At the same time, it is also confirmed that if an inorganic species, whose inhibition against general corrosion is derived from its role for the surface passivation of carbon steel, its addition into chloride solution can induce the initiation of PC for carbon steel. The related report of the above result has been mentioned in Na3BO4 + NaCl solution [4], Na3PO4 + NaCl solution [6], NaNO2 + NaCl solution [9], Na2WO4 + NaCl solution [11], Na2MoO4 + NaCl solution [25] and so on. Further, from the above reports, it is concluded that for carbon steel in chloride solution containing inorganic species, particularly inorganic species with a certain degree of oxidation ability, the occurrence of PC for carbon steel results from the combined actions of Cl and inorganic species, and their appropriate proportion plays a critical role in the initiation of PC.
In our previous works [33,34,35], for Q235 carbon steel in pure Na2WO4 or/and Na2MoO4 solutions free of Cl, we investigated its electrochemical behavior and surface passivation and summarized some rules about the influences of WO42− and MoO42− on its corrosion and passivation behaviors. Both WO42− and MoO42− could promote the surface passivation of the Q235 carbon steel, which was due to their influence on the composition and microstructure of the passive film. However, due to the absence of an aggressive anion, particularly Cl, in pure Na2WO4 or/and Na2MoO4 solutions, the occurrence of PC for Q235 carbon steel is avoided [36]. Further, in the presence of Cl, for carbon steel, in Na2WO4 + NaCl solution, Gao et al. [11] reported that the inhibition of WO42− on the initiation of PC was attributed to its role in promoting the formation of γ-Fe2O3, which was the main composition of the passive film on the carbon steel surface. Jabeera et al. [37] reported that the presence of WO42− resulted in the formation of FeWO4, which repaired the defect of the passive film because of the preferential deposition of FeWO4 at the defect sites. Fujioka et al. [38] reported that the pitting potential and repassivation potential of carbon steel moved to the positive direction with the increase inWO42− concentration, and the role of WO42− resulted from repairing the defect of the passive film and from inhibiting the development of the corrosion pit. At the same time, for carbon steel in Na2MoO4 + NaCl solution, Zhao et al. [23] reported that the presence of MoO42− restrained the nucleation and development of the corrosion pit, which was attributed to the pH value of the pit interior raised with the increase inMoO42− concentration. Zhou et al. [25] reported that the inhibition of MoO42− on PC initiation was due to the role of MoO42− to promote the transformation from FeOOH to Fe2O3 in the passive film and to further enhance the stability of the passive film. Fujioka et al. [38] also reported the influence of MoO42− concentration on the pitting potential and repassivation potential and its role in repairing the passive film defect. Saremi et al. [39] reported that the adsorption and reduction of MoO42− was beneficial to the high resistance and low permeability of the passive film.
As stated above, in the single presence of WO42− or MoO42− in chloride solution, its role and mechanism on the PC inhibition of carbon steel has been greatly reported; however, the synergistic role and mechanism of WO42− and MoO42− on PC inhibition, particularly on the inhibition of PC initiation, of carbon steel are absent. In this work, Na2WO4, Na2MoO4 and NaCl are introduced into de-ionized water to obtain three solutions: WO42− + Cl solution, MoO42− + Cl solution and WO42− + MoO42− + Cl solution. In the above three solutions, the synergistic inhibitions of WO42− and MoO42−, including the inhibitive role and mechanism, on the initiation of PC for Q235 carbon steel are investigated with electrochemical and surface techniques.

2. Materials and Methods

The investigated material of this work was Q235 carbon steel with the following chemical composition (weight percent): C, 0.160; Mn, 0.530; P, 0.015; S, 0.045; Si, 0.300; and Fe, balance. Q235 carbon steel was processed into some samples with the three-dimensional size of 10 × 10 × 3 mm; after that, all samples were manually abraded up to 1000 grit with SiC abrasive paper, rinsed with de-ionized water and degreased in alcohol.
There were three solutions investigated in this work: besides Na+, Solution I comprising WO42− and Cl, Solution II comprising MoO42− and Cl, and Solution III comprising WO42−, MoO42− and Cl. The detailed information of the three solutions, including component and pH value, are listed in Table 1. Solutions I, II and III were prepared with analytical grade agents and de-ionized water.
The measurements of electrochemical techniques, including open circuit potential (OCP) evolution, potentiodynamic polarization, electrochemical impedance spectroscopy (EIS) and Mott–Schottky plot, were carried out by a Princeton 2273 electrochemical workstation (USA) at room temperature (RT). A typical three-electrode system was applied for electrochemical measurements: working electrode was a sample of the Q235 carbon steel, counter electrode was a platinum sheet, and reference electrode was a saturated calomel electrode (SCE). Before each electrochemical test, the surface area of the working electrode (a sample of the Q235 carbon steel) was restricted into a square with the two-dimensional size of 2 × 2 mm with room-temperature-cured silicone rubber. In OCP evolution tests, the record frequency of OCP was 5 Hz; in potentiodynamic polarization tests, the scanning rate of applied potential was 0.5 mV/s; in EIS tests, a perturbation potential of 10 mV amplitude was performed in the frequently range from 105 to10−2 Hz; in Mott–Schottky plot tests, the scanning rate of applied potential was 5 mV/s, and the scanning range of applied potential was from −0.2 to 1.0 VSCE. However, all potentiodynamic polarization tests were terminated when corresponding current density increased suddenly and sharply, and thus, their potential scanning ranges were not proposed in this work.
The measurements of surface techniques included spatial potential distribution and surface chemical composition: a former test was performed by an XMU-BY electrochemical scanning tunneling microscope (ESTM) instrument (Xiamen Legang Materials Technology Co., Ltd., Xiamen, China), and a latter test was conducted by an ESCALAB-250 X-ray photoelectron spectroscopy (XPS) instrument (Waltham, MA, USA).

3. Results and Discussion

3.1. OCP Evolution

Figure 1 shows the OCP evolutions of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions. For Q235 samples in three solutions, with the extension of test time, OCP moves to the positive direction from 0 to 10 min; after that, from 10 to 20 min, the change of OCP is slight. Therefore, prior to the subsequent electrochemical measurements of potentiodynamic polarization, EIS and Mott–Schottky plot, Q235 samples were immersed in corresponding solutions for 20 min to ensure the stability of OCP.
However, the stable OCP value of the Q235 carbon steel in WO42− + Cl, MoO42− + Cl or WO42− + MoO42− + Cl solution increases in turn. For carbon steels in alkaline environments at open circuit condition, anodic half-reaction is the oxidation of an iron element from Fe to Fe2+ with the standard potential (Es) of −0.684 VSCE [40]:
Fe → Fe2+ + 2e
The equilibrium potential (Ee) of Fe oxidation is described as follows:
Ee (Fe2+/Fe) = (−0.684 + 0.059/2 log αFe2+) VSCE
At the same time, cathodic half-reaction is the reduction of an oxygen element from O2 to OH with the Es of −0.157 VSCE [41]:
O2 + 2H2O + 4e → 4OH
The Ee of O2 reduction is described as follows:
Ee (O2/OH) = (0.984 − 0.059 pH) VSCE
In three solutions, their same pH value suggests the approximate Ee of O2 reduction; therefore, according to Nernst theory, the difference in a stable OCP value is mainly attributed to the different Ee of Fe oxidation. In the subsequent result of potentiodynamic polarization, it will be seen that in WO42− + Cl, MoO42− + Cl or WO42− + MoO42− + Cl solution, the corrosion current density of the Q235 carbon steel decreases in turn, indicating that Fe2+ concentration near the solution/electrode interface decreases in turn. According to Equation (2), it can be calculated that in WO42− + Cl, MoO42− + Cl or WO42− + MoO42− + Cl solution, the Ee of Fe oxidation moves to the positive direction in turn, resulting in the stable OCP value of the Q235 carbon steel that increases in turn.

3.2. Potentiodynamic Polarization

Figure 2 shows the polarization curve of the Q235 sample in 0.1 mM NaCl solution and the cyclic polarization curves of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions. For the Q235 sample in 0.1 mM NaCl solution, anodic current density increases persistently with the positive shift of applied potential, indicating that Q235 carbon steel presents the electrochemical behavior of activation in 0.1 mM NaCl solution [42]. In contrast, for Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions, with the positive shift of applied potential, anodic current density firstly increases slowly from the corrosion potential (Ec) to approximately −0.3 VSCE, then maintains steadily from −0.3 VSCE to the pitting potential (Ep), and finally increases rapidly when the applied potential is up to Ep. Q235 carbon steel presents the electrochemical behavior of activation–passivation–pitting in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions [43].
However, the influence of solution component on Ec and corrosion current density (ic) is negligible, but on Ep and repassivation potential (Er), it is very significant. Table 2 lists the calculated values of Ec, ic, Ep and Er, in which each Ec, ic, Ep or Er datum is the average value from ten parallel potentiodynamic polarization tests. For Q235 carbon steel in three solutions, the values of Ep and (EpEr) in WO42− + MoO42− + Cl solution are respectively larger and smaller than those in WO42− + Cl or MoO42− + Cl solution, indicating that WO42− and MoO42− show a synergistic role for the inhibition of PC initiation [44]. Because the main aim of this work is to reveal the synergistic role and mechanism of WO42− and MoO42− on the inhibition of PC initiation, the following discussion of this work is mainly focused on physical and chemical properties about the surface of the Q235 carbon steel at the applied potential of Ep.

3.3. Spatial Potential Distribution (SPD)

In order to obtain spatial electrochemical information of PC initiation and propagation, the applied potentials of 0.01, 0.09 and 0.17 VSCE, respectively, being very close to the Ep of the Q235 carbon steel in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions, are exerted on the working electrode artificially.
Figure 3 shows the SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at the applied potential of 0.01 VSCE. At 0.01 VSCE, in the WO42− + Cl solution shown in Figure 3a, an active pitting site with the peak potential of 1.22 mV is detected at the bottom right corner of ESTM tip scanning region, suggesting the initiation of a corrosion pit [45]; by contrast, in the MoO42− + Cl solution shown in Figure 3b and in the WO42− + MoO42− + Cl solution shown in Figure 3c, no obvious active pitting sites are observed in the ESTM tip scanning region.
Figure 4 shows the SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at the applied potential of 0.09 VSCE. In WO42− + Cl solution, both the peak potential and affected region of the active pitting sites at 0.09 VSCE are larger than those at 0.01 VSCE, as shown in Figure 4a and Figure 3a, indicating the end of PC initiation and the beginning of PC propagation [46]. At 0.09 VSCE, in the MoO42− + Cl solution shown in Figure 4b, an active pitting site with the peak potential of 1.16 mV is detected at the top right corner of the ESTM tip scanning region; in the WO42− + MoO42− + Cl solution shown in Figure 4c, no obvious active pitting sites are observed in the ESTM tip scanning region.
Figure 5 shows the SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at the applied potential of 0.17 VSCE. In WO42− + Cl solution, both the peak potential and affected region of the active pitting sites at 0.17 VSCE further increase compared with those at 0.09 and 0.01 VSCE, as shown in Figure 3a, Figure 4a and Figure 5a, suggesting the continuous propagation of PC [47]. In MoO42− + Cl solution, both the peak potential and affected region of the active pitting sites at 0.17 VSCE are larger than those at 0.09 VSCE, as shown in Figure 4b and Figure 5b; at 0.17 VSCE, in the WO42− + MoO42− + Cl solution shown Figure 5c, an active pitting site with the peak potential of 1.06 mV is detected at the middle position of the ESTM tip scanning region.
From the above results of polarization and SPD, on the one hand, the Ep of the Q235 carbon steel in WO42− + MoO42− + Cl solution is more positive than that in WO42− + Cl or MoO42− + Cl solution; on the other hand, at each Ep, both the peak potential and affected region of the active pitting sites in WO42− + MoO42− + Cl solution are smaller than those in WO42− + Cl or MoO42− + Cl solution. The above two aspects conclude that for Q235 carbon steel in Cl solution, the inhibitive role of WO42− and MoO42− on PC initiation when both are used together is better than that when one is used solely.

3.4. XPS

Figure 6 shows the wide-scan XPS of the Q235 samples polarized to Ep in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions. For Q235 samples in three solutions, four peaks, Fe 2p at about 711 eV, O 1s at about 531 eV, C 1s at about 286 eV and Fe 3p at about 55 eV, are gathered by XPS analysis, which is independent of the solution component. Besides the above XPS peaks, W 4d peak at about 247 eV as well as W 4f peak at about 36 eV in WO42− + Cl solution, Mo 3d peak at about 235 eV in MoO42− + Cl solution, and W 4d peak at about 247 eV, Mo 3d peak at about 235 eV as well as W 4f peak at about 37 eV in WO42− + MoO42− + Cl solution are also gathered by XPS analysis. The result of wide-scan XPS indicates that the passive film of the Q235 carbon steel formed in the three solutions has different chemical composition.
Figure 7 shows the high-resolution XPS of Fe 2p for Q235 samples polarized to Ep in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions. In the WO42− + Cl solution shown in Figure 7a, the Fe 2p spectrum of the Q235 sample reveals three peaks at 712.05, 710.85 and 706.95 eV, respectively, corresponding to the Fe element in the valence states of Fe3+, Fe2+ and Fe0 [48]; in MoO42− + Cl solution shown in Figure 7b and in WO42− + MoO42− + Cl solution shown in Figure 7c, each Fe 2p spectrum also reveals three peaks corresponding to Fe3+, Fe2+ and Fe0. However, the intensity of the Fe3+ peak in MoO42− + Cl and WO42− + MoO42− + Cl solutions is obviously stronger than that in WO42− + Cl solution; conversely, the intensities of Fe2+ and Fe0 are weaker in MoO42− + Cl and WO42− + MoO42− + Cl solutions than in WO42− + Cl solution. This result implies that the oxidation ability of MoO42− is stronger than that of WO42−, which is also reported regarding their oxidation for stainless steel [49] and cold rolling steel [50], similarly.
In this work, the relatively strong oxidation ability of MoO42− plays an important role in the synergistic inhibitions of WO42− and MoO42−. In the subsequent results of EIS and the Mott–Schottky plot, it will be seen that the passive film of the Q235 carbon steel formed in WO42− + MoO42− + Cl solution has larger passive film resistance and a smaller passive film defect than that formed in WO42− + Cl or MoO42− + Cl solution, which is very closely associated with the relatively high content of Fe3+ in the passive film. On the other hand, according to bipolar model [51], more Fe3+ and less Fe2+ transfer across the passive film from an anion-selective type to a cation-selective type, which is beneficial to prevent passive film from the adsorption and attack of Cl.
Figure 8 shows the high-resolution XPS of W 4f for Q235 samples polarized to Ep in WO42− + Cl and WO42− + MoO42− + Cl solutions. The W 4f spectrum of the Q235 sample exhibits the spin-orbit splitting double peaks of 37.50 eV as well as 35.40 eV in WO42− + Cl solution and 37.55 eV as well as 35.15 eV in WO42− + MoO42− + Cl solution, indicating that the W element is present in the passive film of the Q235 carbon steel formed in WO42− + Cl and WO42− + MoO42− + Cl solutions.
Figure 9 shows the high-resolution XPS of Mo 3d for Q235 samples polarized to Ep in MoO42− + Cl and WO42− + MoO42− + Cl solutions. Similar to W 4f, Mo 3d also exhibits spin-orbit splitting double peaks: at 235.70 and 232.40 eV in MoO42− + Cl solution, and at 235.80 and 232.70 eV in WO42− + MoO42− + Cl solution.
When carbon steels are exposed in an atmosphere environment, an air-formed passive film forms on their surface spontaneously [52]; further, when served in alkaline environments, previous passive film formed in air can rearrange a double-layer microstructure [53]. The inner dense layer of the passive film is composed of FeOOH and Fe2O3, and the outer loose layer of the passive film is composed of Fe(OH)2·nH2O and Fe(OH)3·nH2O [54]. The related mechanism of the above statement is as follows [55]:
Fe + OH → FeOHads
FeOHads → FeOHads + e
FeOHads + OH → Fe(OH)2 + e
Fe(OH)2 + OH → FeOOH + H2O + e
Although there are many defects in the outer loose layer of the passive film [56], some introduced substances, such as WO42− and MoO42−, can repair them [49,50]. According to the present XPS results and our previous works [33,34,35], it is concluded that besides iron oxides and iron hydroxides, the passive film of the Q235 carbon steel formed in WO42− + Cl, MoO42− + Cl, or WO42− + MoO42− + Cl solution also comprises FeWO4 plus Fe2(WO4)3, Fe2(MoO4)3, or Fe2(WO4)3 plus Fe2(MoO4)3, respectively. The detailed composition of the passive film on the surface of the Q235 carbon steel formed in three solutions is listed in Table 3.

3.5. EIS

Figure 10 shows the EIS of the Q235 samples in 0.1 mM NaCl solution and in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions. For the Q235 sample in 0.1 mM NaCl solution, the corresponding EIS is composed of only one capacitive semicircle in the entire frequency zone; in contrast, for Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions, each EIS is composed of a relatively small capacitive semicircle in the high-frequency zone and another relatively large capacitive semicircle in the low-frequency zone. In the passivation system of the electrode/electrolyte, the appearance of the capacitive semicircle in EIS mainly results from the formation of the passive film on the interface between the electrode and electrolyte [57]. The present EIS results of the two capacitive semicircles confirm the double-layer microstructure of the passive film, and it is reasonable to infer that the small capacitive semicircle of EIS is attributed to the inner dense layer of the passive film, and another large one is due to the outer loose layer [35].
However, the influence of the solution component on the radius of the capacitive semicircle in the high-frequency zone is slight, but on that in the low-frequency zone, it is severe. That is to say, for the Q235 carbon steel in three solutions, the inhibitive role and mechanism of WO42− and MoO42− on PC initiation are mainly derived from their influence on the outer loose layer of the passive film, rather than to the inner dense layer. The radius of the large capacitive semicircle in WO42− + Cl, MoO42− + Cl or WO42− + MoO42− + Cl solutions enlarges in turn, indicating that the corrosion resistance of the outer loose layer for the Fe2(WO4)3 plus Fe2(MoO4)3 film is better than that for the FeWO4 plus Fe2(WO4)3 film or Fe2(MoO4)3 film.
Further, the method of equivalent electrical circuit (EEC) fitting is applied to interpret EIS. Combining the EIS results shown in Figure 10 and our predecessors’ research studies [58], the model of EEC shown in Figure 11 is feasible to EIS interpretation. In Figure 11, Rs represents solution resistance; CPEo and Ro respectively represent the capacitance and resistance of the outer loose layer in the passive film; CPEi and Ri represent the capacitance and resistance of the inner dense layer in the passive film, respectively.
Table 4 lists the fitted values of CPEo, Ro, CPEi and Ri, in which each CPEo, Ro, CPEi or Ri datum is the average value from ten parallel EIS tests. It was reported that the value of the passive film resistance reflected the anti-corrosion protection of the passive film, and the larger the resistance, the better the anti-corrosion protection [32]; the value of the passive film capacitance indicated the damaged area of the passive film, and the larger the capacitance, the more severe the film damage [57]. For Q235 carbon steel in WO42− + Cl, MoO42− + Cl or WO42− + MoO42− + Cl solution, the values of CPEo and Ro change obviously, but the values of CPEi and Ri change slightly, confirming that for the passive film, the influence of WO42− and MoO42− on its outer loose layer is greater than that on its inner dense layer; on the other hand, the value of CPEo decreases, and the value of Ro increases in turn, indicating that the Fe2(WO4)3 plus Fe2(MoO4)3 film shows better corrosion resistance against PC than the FeWO4 plus Fe2(WO4)3 film or Fe2(MoO4)3 film.

3.6. Mott–Schottky Plot

Figure 12 shows the Mott–Schottky plots of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions. For the Q235 samples in three solutions, the slope of the straight line part for each Mott–Schottky plot exhibits a positive value, suggesting that the FeWO4 plus Fe2(WO4)3 film, Fe2(MoO4)3 film and Fe2(WO4)3 plus Fe2(MoO4)3 film satisfy the property of the n-type semiconductor [59]. It is generally accepted that for the passive film of n-type characteristic, its Mott–Schottky plot can be interpreted with the following equation [60]:
C−2 = 2(EUf − kT/e)/εε0eND
In Equation (9), C represents space charge layer capacitance, E represents applied potential, Uf represents flat band potential, k is Boltzmann constant, T is absolute temperature, e is electron charge, ε represents passive film permittivity, ε0 is free space permittivity, and ND represents donor density. Therein, the value of ND can reflect the defect quantity of the passive film: the larger the ND of the numerical value, the more defects in the passive film; at the same time, the value of Uf can reflect the corrosion susceptibility of the working electrode in the electrolyte, similar to that of Ec [61].
The influence of the solution component on ND is greater than that on Uf, and Table 5 lists the fitted values of ND and Uf, in which each ND or Uf datum is the average valuefrom ten parallel Mott–Schottky plot tests. For Q235 carbon steel in WO42− + Cl, MoO42− + Cl or WO42− + MoO42− + Cl solution, the value of ND increases in turn, indicating that the Fe2(WO4)3 plus Fe2(MoO4)3 film takes along smaller defects than the FeWO4 plus Fe2(WO4)3 film and Fe2(MoO4)3 film [61]; the value of Uf changes slightly, which is similar to the value of Ec, implying that Q235 carbon steel presents the approximate characteristic of uniform corrosion in three solutions.
In our predecessors’ research studies on PC, there are many theories and models proposed to reveal the initiation of a corrosion pit, such as acidification theory [62], chemical dissolution theory [63], depassivation–repassivation theory [64], anion penetration/migration model [65], chemical–mechanical model [66] and point defect model [67]. However, in the above theories and models [62,63,64,65,66,67], a critical step of PC initiation, the adsorption and the attack of aggressive anions on the surface of the passive film, was approved consistently by our predecessors. On the passive film, defective sites were more likely to be adsorbed and attacked by aggressive anions than other regions [1]. From the above results of EIS and Mott–Schottky plot, for the FeWO4 plus Fe2(WO4)3 film, Fe2(MoO4)3 film and Fe2(WO4)3 plus Fe2(MoO4)3 film, the film resistance (Ri+Ro) increases and the defect quantity decreases in turn. Therefore, the Fe2(WO4)3 plus Fe2(MoO4)3 film has a better capability to resist the adsorption and attack of Cl than FeWO4 plus Fe2(WO4)3 film or Fe2(MoO4)3 film [68], and WO42− and MoO42− exhibit a better inhibitive role on PC initiation when both are used together than when one is used solely.

4. Conclusions

(1)
In Cl solution, the simultaneous additions of WO42− and MoO42− showed better inhibition on PC initiation than the single addition of WO42− or MoO42−, and the synergistic role between WO42− and MoO42− for the inhibition of PC initiation was present.
(2)
Besides iron oxides and iron hydroxides, the passive film of Q235 carbon steel was also composed of FeWO4 plus Fe2(WO4)3 in WO42− + Cl solution, of Fe2(MoO4)3 in MoO42− + Cl solution and of Fe2(WO4)3 plus Fe2(MoO4)3 in WO42− + MoO42− + Cl solution.
(3)
The synergistic mechanism between WO42− and MoO42− for the inhibition of PC initiation was that the Fe2(WO4)3 plus Fe2(MoO4)3 film showed larger film resistance and smaller defect quantity than the FeWO4 plus Fe2(WO4)3 film and Fe2(MoO4)3 film.

Author Contributions

Conceptualization, H.Y.; methodology, Y.Z.; software, P.Z.; validation, H.Y., P.Z., G.N. and Y.Z.; formal analysis, H.Y.; investigation, G.N.; resources, H.Y.; data curation, Y.Z.; writing—original draft preparation, H.Y.; writing—review and editing, Y.Z.; visualization, P.Z.; supervision, G.N.; project administration, H.Y.; funding acquisition, H.Y. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the Scientific Research Start-up Project of High Level Talents in Yulin Normal University (G2019ZK53), the National Natural Science Foundaton of China (22266017), the Doctoral Scientific Research Start-up Project of Jinggangshan University (JZB2201), the Guangxi Innovation Driven Development Major Project (Guike AA20302013) and the “Yongjing Plan” Project of Leading Talents of Innovation and Entrepreneurship in Nanning City (no. 2020024).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Soltis, J. Passivity breakdown, pit initiation and propagation of pits in metallic materials—Review. Corros. Sci. 2015, 90, 5–22. [Google Scholar] [CrossRef]
  2. Zhou, Y.; Zuo, Y. The inhibitive mechanisms of nitrite and molybdate anions on initiation and propagation of pitting corrosion for mild steel in chloride solution. Appl. Surf. Sci. 2015, 353, 924–932. [Google Scholar] [CrossRef]
  3. Shang, Z.; Zhu, J.Y. Overview on plant extracts as green corrosion inhibitors in the oil and gas fields. J. Mater. Res. Technol. 2021, 15, 5078–5094. [Google Scholar] [CrossRef]
  4. Zhou, Y.; Xiong, J.P.; Yan, F.A. The preparation and characterization of a nano-CeO2/phosphate composite coating on magnesium alloy AZ91D. Surf. Coat. Technol. 2017, 328, 335–343. [Google Scholar] [CrossRef]
  5. Wang, J.X.; Han, L.; Liu, Z.; Wang, D.M. Setting controlling of lithium slag-based geopolymer by activator and sodium tetraborate as a retarder and its effects on mortar properties. Cem. Concr. Compos. 2020, 110, 103598. [Google Scholar] [CrossRef]
  6. Zuo, Y.; Wang, H.T.; Zhao, J.M.; Xiong, J.P. The effects of some anions on metastable pitting of 316L stainless steel. Corros. Sci. 2002, 44, 13–24. [Google Scholar] [CrossRef]
  7. Zakeri, M.; Nakhaie, D.; Naghizadeh, M.; Moayed, M.H. The effect of dichromate ion on the pitting corrosion of AISI 316 stainless steel. Part I: Critical pitting temperature. Corros. Sci. 2015, 93, 234–241. [Google Scholar] [CrossRef]
  8. Emregul, K.C.; Aksut, A.A. The effect of sodium molybdate on the pitting corrosion of aluminum. Corros. Sci. 2003, 45, 2415–2433. [Google Scholar] [CrossRef]
  9. Dong, Z.H.; Shi, W.; Guo, X.P. Initiation and repassivation of pitting corrosion of carbon steel in carbonated concrete pore solution. Corros. Sci. 2011, 53, 1322–1330. [Google Scholar] [CrossRef]
  10. Lu, X.Y.; Zhang, L.Y.; Feng, X.G.; Chen, D.; Zuo, Y. Effect of aluminum tripolyphosphate on pitting initiation on carbon steel in chloride contaminated concrete pore solution. Anti-Corros. Methods Mater. 2019, 66, 603–612. [Google Scholar] [CrossRef]
  11. Zhou, Y.; Zhang, P.; Su, L.H.Z.; Fan, B.M.; Yan, F.A. One-step preparation and characterization of a Ce-La-Y ternary rare earth conversion coating on magnesium alloy AZ91D. Mater. Lett. 2021, 304, 130640. [Google Scholar] [CrossRef]
  12. Rodriguez, J.; Mouanga, M.; Roobroeck, A.; Cossement, D.; Mirisola, A.; Olivier, M.-G. Study of the inhibition ability of benzotriazole on the Zn-Mg coated steel corrosion in chloride electrolyte. Corros. Sci. 2018, 132, 56–67. [Google Scholar] [CrossRef]
  13. Wang, Y.S.; Zuo, Y.; Zhao, X.H.; Zha, S.S. The adsorption and inhibition effect of calcium lignosulfonate on Q235 carbon steel in simulated concrete pore solution. Appl. Surf. Sci. 2016, 379, 98–110. [Google Scholar] [CrossRef]
  14. Tan, Y.J.; Mocerino, M.; Paterson, T. Organic molecules showing the characteristics of localised corrosion aggravation and inhibition. Corros. Sci. 2011, 53, 2041–2045. [Google Scholar] [CrossRef]
  15. Zuo, Y.; Wang, S.W.; Tang, Y.M.; Zhou, Y. The inhibition of sodium oleate for pitting corrosion of aluminum alloy 2024 in 0.1 mol L-1 NaCl solution. J. Braz. Chem. Soc. 2015, 26, 1656–1663. [Google Scholar]
  16. Zhou, B.E.; Wang, Y.S.; Zuo, Y. Evolution of the corrosion process of AA 2024-T3 in an alkaline NaCl solution with sodium dodecylbenzenesulfonate and lanthanum chloride inhibitors. Appl. Surf. Sci. 2015, 357, 735–744. [Google Scholar] [CrossRef]
  17. Li, Y.; Lu, X.P.; Wu, K.X.; Yang, L.; Zhang, T.; Wang, F.H. Exploration the inhibition mechanism of sodium dodecyl sulfate on Mg alloy. Corros. Sci. 2020, 168, 108559. [Google Scholar] [CrossRef]
  18. Wang, Y.S.; Zuo, Y.; Tang, Y.M. Inhibition effect and mechanism of sodium oleate on passivation and pitting corrosion of steel in simulated concrete pore solution. Constr. Build. Mater. 2018, 167, 197–204. [Google Scholar] [CrossRef]
  19. Tan, Y.J.; Fwu, Y.; Bhardwaj, K. Electrochemical evaluation of under-deposit corrosion and its inhibition using the wire beam electrode method. Corros. Sci. 2011, 53, 1254–1261. [Google Scholar] [CrossRef]
  20. Zhou, Y.; Zhang, P.; Yan, F.A. Corrosion resistance of a nano-Mg modified silane conversion coating with cathodic protection on magnesium alloy AZ91D. Mater. Lett. 2021, 284, 128930. [Google Scholar] [CrossRef]
  21. Deyab, M.A. Electrochemical investigations on pitting corrosion inhibition of mild steel by provitamin B5 in circulating cooling water. Electrochim. Acta 2016, 202, 262–268. [Google Scholar] [CrossRef]
  22. Tang, Y.M.; Zhao, X.H.; Mao, J.P.; Zuo, Y. The electrochemical characteristics of pitting for two steels in phosphate buffer solution with chloride. Mater. Chem. Phys. 2009, 116, 484–488. [Google Scholar] [CrossRef]
  23. Zhao, J.M.; Zuo, Y. The effects of molybdate and dichromate anions on pit propagation of mild steel in bicarbonate solution containing Cl. Corros. Sci. 2002, 44, 2119–2130. [Google Scholar] [CrossRef]
  24. Al-Refaie, A.A.; Walton, J.; Cottis, R.A.; Lindsay, R. Photoelectron spectroscopy study of the inhibition of mild steel corrosion by molybdate and nitrite anions. Corros. Sci. 2010, 52, 422–428. [Google Scholar] [CrossRef]
  25. Zhou, Y.; Zuo, Y.; Bin, L. The compounded inhibition of sodium molybdate and benzotriazole on pitting corrosion of Q235 steel in NaCl + NaHCO3 solution. Mater. Chem. Phys. 2017, 192, 86–93. [Google Scholar] [CrossRef]
  26. Lin, B.; Zuo, Y. Inhibition of Q235 carbon steel by calcium lignosulfonate and sodium molybdate in carbonated concrete pore solution. Molecules 2019, 24, 518. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  27. Zuo, Y.; Yang, L.; Tan, Y.J.; Wang, Y.S.; Zhao, J.M. The effects of thioureido imidazoline and NaNO2 on passivation and pitting corrosion of X70 steel in acidic NaCl solution. Corros. Sci. 2017, 120, 99–106. [Google Scholar] [CrossRef]
  28. Dong, Z.H.; Shi, W.; Zhang, G.A.; Guo, X.P. The role of inhibitors on the repassivation of pitting corrosion of carbon steel in synthetic carbonated concrete pore solution. Electrochim. Acta 2011, 56, 5890–5897. [Google Scholar] [CrossRef]
  29. Lin, B.; Tang, J.L.; Wang, Y.Y.; Wang, H.; Zuo, Y. Study on synergistic corrosion inhibition effect between calcium lignosulfonate (CLS) and inorganic inhibitors on Q235 carbon steel in alkaline environment with Cl. Molecules 2020, 25, 4200. [Google Scholar] [CrossRef]
  30. Wang, Y.S.; Zuo, Y. The adsorption and inhibition behavior of two organic inhibitors for carbon steel in simulated concrete pore solution. Corros. Sci. 2017, 118, 24–30. [Google Scholar] [CrossRef]
  31. Han, P.; Chen, C.F.; Yu, H.B.; Zheng, Y.J. Study of pitting corrosion of L245 steel in H2S environments induced by imidazoline quaternary ammonium salts. Corros. Sci. 2016, 112, 128–137. [Google Scholar] [CrossRef]
  32. Chen, X.; Xiong, Q.Y.; Zhu, F.; Li, H.; Liu, D.; Xiong, J.P.; Zhou, Y. The effects of chloride anions on corrosion and passivation behavior of 254SMO stainless steel in water absorbed of blast furnace gas (BFG). Int. J. Electrochem. Sci. 2018, 13, 1656–1665. [Google Scholar] [CrossRef]
  33. Zhang, P.; Chen, Y.J.; Huang, H.J.; Zhou, Y.; Yan, F.A.; Nie, G.C. Surface passive film characteristic of Q235 carbon steel in pure molybdate solution. Surf. Rev. Lett. 2020, 27, 1950179. [Google Scholar] [CrossRef]
  34. Chen, Y.J.; Zhang, P.; Zhou, Y.; Yan, F.A. The role of WO42− on surface passivation for Q235 carbon steel in tungstate solution. Anti-Corros. Methods Mater. 2020, 67, 483–489. [Google Scholar] [CrossRef]
  35. Zhang, P.; Chen, Y.J.; Zhou, Y.; Yan, F.A.; Nie, G.C. Electrochemical investigation of the synergistic effect between molybdate and tungstate on surface passivation of carbon steel. Int. J. Electrochem. Sci. 2021, 16, 151027. [Google Scholar] [CrossRef]
  36. Zhou, Y.; Yan, F.A. The relation between intergranular corrosion and electrochemical characteristic of carbon steel in carbonic acid and sodium nitrite solutions. Int. J. Electrochem. Sci. 2016, 16, 3976–3986. [Google Scholar] [CrossRef]
  37. Jabeera, B.; Shibli, S.M.A.; Anirudham, T.S. Synergistic inhibitive effect of tartarate and tungstate in preventing steel corrosion in aqueous media. Appl. Surf. Sci. 2006, 252, 3520–3524. [Google Scholar] [CrossRef]
  38. Fujioka, E.; Nishihara, H.; Aramaki, K. The inhibition of pit nucleation and growth on the passive surface of iron in a borate buffer solution containing Cl− by oxidizing inhibitors. Corros. Sci. 1996, 38, 1915–1933. [Google Scholar] [CrossRef]
  39. Saremi, M.; Dehghanian, C.; Sabet, M.M. The effect of molybdate concentration and hydrodynamic effect on mild steel corrosion inhibition in simulated cooling water. Corros. Sci. 2006, 48, 1404–1412. [Google Scholar] [CrossRef]
  40. Zhou, Y.; Zhang, P.; Xiong, J.P.; Yan, F.A. The relationship between activation-passivation transition and grain boundary dissolution on four steel samples in acidic solutions containing NO2. RSC Adv. 2019, 9, 23589–23597. [Google Scholar] [CrossRef] [Green Version]
  41. Li, X.; Zhang, P.; Huang, H.J.; Hu, X.C.; Zhou, Y.; Yan, F.A. An electrochemical study of pH influences on corrosion and passivation for a Q235 carbon steel in HNO3-NaNO2, HAc-NaNO2 and HCl-NaNO2 solutions. RSC Adv. 2019, 9, 39055–39063. [Google Scholar] [CrossRef] [PubMed]
  42. Deng, R.J.; Zhang, P.; Zhao, X.Y.; Cai, G.Y.; Xiong, H.L.J.P.; Zhou, Y. The comparative investigation of corrosion and passivation for X65 carbon steel in pH 1 to 5 HNO3 solutions without and with 0.01 mol L-1 NaNO2. J. Braz. Chem. Soc. 2020, 31, 731–738. [Google Scholar] [CrossRef]
  43. Zhou, Y.; Zhang, P.; Huang, H.J.; Xiong, J.P.; Yan, F.A. The effects of pH values on functional mechanisms of nitrite anions for Q235 carbon steels in 0.01 mol L-1 NaNO2-HCl solutions. J. Braz. Chem. Soc. 2019, 30, 1688–1696. [Google Scholar] [CrossRef]
  44. Tang, Y.M.; Zuo, Y.; Wang, J.N.; Zhao, Z.H.; Niu, B.; Lin, B. The metastable pitting potential and its relation to the pitting potential for four materials in chloride solutions. Corros. Sci. 2014, 80, 111–119. [Google Scholar] [CrossRef]
  45. Lin, B.; Hu, R.G.; Ye, C.Q.; Li, Y.; Lin, C.J. A study on the initiation of pitting corrosion in carbon steel in chloride-containing media using scanning electrochemical probes. Electrochim. Acta 2010, 55, 6542–6545. [Google Scholar] [CrossRef]
  46. Ye, C.Q.; Hu, R.G.; Li, Y.; Lin, C.J.; Pan, J.S. Probing the vertical profiles of potential in a thin layer of solution closed to electrode surface during localized corrosion of stainless steel. Corros. Sci. 2012, 61, 242–245. [Google Scholar] [CrossRef]
  47. Wang, C.; Cai, Y.Z.; Ye, C.Q.; Dong, S.G.; Cai, X.S.; Cao, Y.H.; Lin, C.J. In situ monitoring of the localized corrosion of 304 stainless steel in FeCl3 solution using a joint electrochemical noise and scanning reference electrode technique. Electrochem. Commun. 2018, 90, 11–15. [Google Scholar] [CrossRef]
  48. Zhou, Y.; Zhang, P.; Zuo, Y.; Liu, D.; Yan, F.A. The structure and composition of corrosion product film and its relation to corrosion rate for carbon steels in CO2 saturated solutions at different temperatures. J. Braz. Chem. Soc. 2017, 28, 2490–2499. [Google Scholar] [CrossRef]
  49. Alentejano, C.R.; Aoki, I.V. Localized corrosion inhibition of 304 stainless steel in pure water by oxyanions tungstate and molybdate. Electrochim. Acta 2004, 49, 2779–2785. [Google Scholar] [CrossRef]
  50. Mu, G.N.; Li, X.H.; Qu, Q.; Zhou, J. Molybdate and tungstate as corrosion inhibitors for cold rolling steel in hydrochloric acid solution. Corros. Sci. 2006, 48, 445–459. [Google Scholar] [CrossRef]
  51. Sato, N. Toward a more fundamental understanding of corrosion processes. Corrosion 1989, 45, 354–368. [Google Scholar] [CrossRef]
  52. Zhou, Y.; Huang, H.J.; Zhang, P.; Liu, D.; Yan, F.A. Effects of nitrite anions on surface passive film properties for Q235 carbon steels. Surf. Rev. Lett. 2019, 26, 1850218. [Google Scholar] [CrossRef]
  53. Lee, D.Y.; Kim, W.C.; Kim, J.G. Effect of nitrite concentration on the corrosion behaviour of carbon steel pipelines in synthetic tap water. Corros. Sci. 2012, 64, 105–114. [Google Scholar] [CrossRef]
  54. Hu, X.C.; Zhang, P.; Zhou, Y.; Yan, F.A. The electrochemical behavior of corrosion and passivation for Q235 carbon steel in acidic phosphate buffer solutions without and with NO2. Anti-Corros. Methods Mater. 2020, 67, 473–481. [Google Scholar] [CrossRef]
  55. Valcarce, M.B.; Vazquez, M. Carbon steel passivity examined in alkaline solutions: The effect of chloride and nitrite ions. Electrochim. Acta 2008, 53, 5007–5015. [Google Scholar] [CrossRef]
  56. Foulkes, F.R.; McGrath, P. A rapid cyclic voltammetric method for studying cement factors affecting the corrosion of reinforced concrete. Cem. Concr. Res. 1999, 29, 873–883. [Google Scholar] [CrossRef]
  57. Chen, L.C.; Zhang, P.; Xiong, Q.Y.; Zhao, P.; Xiong, J.P.; Zhou, Y. The influences of chloride anions on corrosion electrochemical characteristics of 904L stainless steel in blast furnace gas/water system. Int. J. Electrochem. Sci. 2019, 14, 919–928. [Google Scholar] [CrossRef]
  58. Deng, F.G.; Wang, L.S.; Zhou, Y.; Gong, X.H.; Zhao, X.P.; Hu, T.; Wu, C.Q. Effect of nanosilica content on the corrosion inhibition of composite coatings of a filled epoxy resin grafted with a hydrophobic fluoroalkylsilane: A dual critical concentrations interpretation. RSC Adv. 2017, 7, 48876–48893. [Google Scholar] [CrossRef] [Green Version]
  59. Cheng, Y.F.; Luo, J.L. Electronic structure and pitting susceptibility of passive film on carbon steel. Electrochim. Acta 1999, 44, 2947–2957. [Google Scholar] [CrossRef]
  60. Ma, Y.C.; Fan, B.M.; Liu, H.; Fan, G.F.; Hao, H.; Yang, B. Enhanced corrosion inhibition of aniline derivatives electropolymerized coatings on copper: Preparation, characterization and mechanism modeling. Appl. Surf. Sci. 2020, 514, 146086. [Google Scholar] [CrossRef]
  61. Li, W.S.; Luo, J.L. Electric properties and pitting susceptibility of passive films formed on iron in chromate solution. Electrochem. Commun. 1999, 1, 349–353. [Google Scholar] [CrossRef]
  62. Galvele, J.R. Transport processes and the mechanism of pitting of metals. J. Electrochem. Soc. 1976, 123, 464–474. [Google Scholar] [CrossRef] [Green Version]
  63. Hoar, T.P.; Jacob, W.R. Breakdown of passivity of stainless steel by halide ions. Nature 1967, 216, 1209–1301. [Google Scholar] [CrossRef]
  64. Dawson, J.L.; Ferreira, M.G.S. Electrochemical studies of the pitting of austenitic stainless steel. Corros. Sci. 1986, 26, 1009–1026. [Google Scholar] [CrossRef]
  65. Okamoto, G. Passive film of 18-8 stainless steel structure and its function. Corros. Sci. 1973, 13, 471–489. [Google Scholar] [CrossRef]
  66. Sato, N. A theory for breakdown of anodic oxide films on metals. Electrochim. Acta 1971, 16, 1683–1692. [Google Scholar] [CrossRef]
  67. Macdonald, D.D. The point defect model for the passive state. J. Electrochem. Soc. 1992, 139, 3434–3449. [Google Scholar] [CrossRef]
  68. Tang, Y.M.; Dun, Y.C.; Chen, X.P.; Zhou, Y.; Zhao, X.H.; Zuo, Y. Electrochemcial impedance spectroscopy characteristic of degradation process for carbon fiber/vinyl ester composites in salt water. J. Compos. Mater. 2022, 56, 1299–1312. [Google Scholar] [CrossRef]
Figure 1. OCP evolutions of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Figure 1. OCP evolutions of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Materials 15 08986 g001
Figure 2. Polarization curve of the Q235 sample in 0.1 mM NaCl solution (a) and cyclic polarization curves of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions (b).
Figure 2. Polarization curve of the Q235 sample in 0.1 mM NaCl solution (a) and cyclic polarization curves of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions (b).
Materials 15 08986 g002
Figure 3. SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at applied potential of 0.01 VSCE: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Figure 3. SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at applied potential of 0.01 VSCE: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Materials 15 08986 g003
Figure 4. SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at applied potential of 0.09 VSCE: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Figure 4. SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at applied potential of 0.09 VSCE: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Materials 15 08986 g004
Figure 5. SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at applied potential of 0.17 VSCE: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Figure 5. SPD images of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions at applied potential of 0.17 VSCE: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Materials 15 08986 g005aMaterials 15 08986 g005b
Figure 6. Wide-scan XPS of the Q235 samples polarized to Ep in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Figure 6. Wide-scan XPS of the Q235 samples polarized to Ep in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Materials 15 08986 g006
Figure 7. High-resolution XPS of Fe 2p for Q235 samples polarized to Ep in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Figure 7. High-resolution XPS of Fe 2p for Q235 samples polarized to Ep in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions: (a) WO42− + Cl solution, (b) MoO42− + Cl solution and (c) WO42− + MoO42− + Cl solution.
Materials 15 08986 g007
Figure 8. High-resolution XPS of W 4f for Q235 samples polarized to Ep in WO42− + Cl and WO42− + MoO42− + Cl solutions: (a) WO42− + Cl solution and (b) WO42− + MoO42− + Cl solution.
Figure 8. High-resolution XPS of W 4f for Q235 samples polarized to Ep in WO42− + Cl and WO42− + MoO42− + Cl solutions: (a) WO42− + Cl solution and (b) WO42− + MoO42− + Cl solution.
Materials 15 08986 g008
Figure 9. High-resolution XPS of Mo 3d for Q235 samples polarized to Ep in MoO42− + Cl and WO42− + MoO42− + Cl solutions: (a) MoO42− + Cl solution and (b) WO42− + MoO42− + Cl solution.
Figure 9. High-resolution XPS of Mo 3d for Q235 samples polarized to Ep in MoO42− + Cl and WO42− + MoO42− + Cl solutions: (a) MoO42− + Cl solution and (b) WO42− + MoO42− + Cl solution.
Materials 15 08986 g009
Figure 10. EIS of the Q235 samples in 0.1 mM NaCl solution (a) and in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions (b).
Figure 10. EIS of the Q235 samples in 0.1 mM NaCl solution (a) and in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions (b).
Materials 15 08986 g010
Figure 11. EEC model for EIS interpretation.
Figure 11. EEC model for EIS interpretation.
Materials 15 08986 g011
Figure 12. Mott–Schottky of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Figure 12. Mott–Schottky of the Q235 samples in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Materials 15 08986 g012
Table 1. Component and pH value of Solution I, Solution II and Solution III.
Table 1. Component and pH value of Solution I, Solution II and Solution III.
SolutionComponentpHDescription
I0.2 mM Na2WO4 + 0.1 mM NaCl8.5WO42− + Cl
II0.2 mM Na2MoO4 + 0.1 mM NaCl8.5MoO42− + Cl
III0.1 mM Na2WO4 + 0.1 mM Na2MoO4 + 0.1 mM NaCl8.5WO42− + MoO42− + Cl
Table 2. Calculated values of Ec, ic, Ep, Er and (EpEr) for Q235 carbon steel in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Table 2. Calculated values of Ec, ic, Ep, Er and (EpEr) for Q235 carbon steel in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
SolutionEc (VSCE)ic (µA/cm2)Ep (VSCE)Er (VSCE)Ep–Er (VSCE)
WO42− + Cl−0.408.160.01−0.250.35
MoO42− + Cl−0.397.520.09−0.050.14
WO42− + MoO42− + Cl−0.386.830.170.060.09
Table 3. Composition of the passive film on Q235 carbon steel surface formed in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Table 3. Composition of the passive film on Q235 carbon steel surface formed in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
SolutionPassive Film CompositionDescription
WO42− + ClFeOOH/Fe2O3, Fe(OH)2, Fe(OH)3, FeWO4, Fe2(WO4)3FeWO4 plus Fe2(WO4)3 film
MoO42− + ClFeOOH/Fe2O3, Fe(OH)2, Fe(OH)3, Fe2(MoO4)3Fe2(MoO4)3 film
WO42− + MoO42− + ClFeOOH/Fe2O3, Fe(OH)2, Fe(OH)3, Fe2(WO4)3, Fe2(MoO4)3Fe2(WO4)3 plus Fe2(MoO4)3 film
Table 4. Fitted values of CPEo, Ro, CPEi and Ri for Q235 carbon steel in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Table 4. Fitted values of CPEo, Ro, CPEi and Ri for Q235 carbon steel in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
SolutionCPEo (μF/cm2)Ro (kΩ cm2)CPEi (μF/cm2)Ri (kΩ cm2)
WO42− + Cl372.5889.5826.435.44
MoO42− + Cl258.47148.7325.075.13
WO42− + MoO42− + Cl140.21179.5823.925.67
Table 5. Fitted values of ND and Uf for Q235 carbon steel in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
Table 5. Fitted values of ND and Uf for Q235 carbon steel in WO42− + Cl, MoO42− + Cl and WO42− + MoO42− + Cl solutions.
SolutionND (cm−3)Uf (VSCE)
WO42− + Cl4.16 × 1018−0.08
MoO42− + Cl3.83 × 1018−0.05
WO42− + MoO42− + Cl1.92 × 1018−0.01
Publisher’s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Share and Cite

MDPI and ACS Style

Yang, H.; Zhang, P.; Nie, G.; Zhou, Y. The Synergistic Inhibitions of Tungstate and Molybdate Anions on Pitting Corrosion Initiation for Q235 Carbon Steel in Chloride Solution. Materials 2022, 15, 8986. https://0-doi-org.brum.beds.ac.uk/10.3390/ma15248986

AMA Style

Yang H, Zhang P, Nie G, Zhou Y. The Synergistic Inhibitions of Tungstate and Molybdate Anions on Pitting Corrosion Initiation for Q235 Carbon Steel in Chloride Solution. Materials. 2022; 15(24):8986. https://0-doi-org.brum.beds.ac.uk/10.3390/ma15248986

Chicago/Turabian Style

Yang, Huanggen, Pei Zhang, Guochao Nie, and Yong Zhou. 2022. "The Synergistic Inhibitions of Tungstate and Molybdate Anions on Pitting Corrosion Initiation for Q235 Carbon Steel in Chloride Solution" Materials 15, no. 24: 8986. https://0-doi-org.brum.beds.ac.uk/10.3390/ma15248986

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop