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Article

Study on Electrochemical Corrosion of Q235 Steel in Sand Containing HA Solution under a Natural Air-Dried State

1
Department of Materials Science and Engineering, Jinzhong University, Jinzhong 030600, China
2
College of Civil Engineering, Taiyuan University of Technology, Taiyuan 030024, China
3
College of Materials Science and Engineering, Taiyuan University of Technology, Taiyuan 030024, China
4
Material Corrosion and Protection Key Laboratory of Sichuan Province, Sichuan University of Science and Engineering, Zigong 643002, China
*
Author to whom correspondence should be addressed.
Coatings 2024, 14(4), 491; https://doi.org/10.3390/coatings14040491
Submission received: 24 February 2024 / Revised: 8 April 2024 / Accepted: 12 April 2024 / Published: 16 April 2024
(This article belongs to the Special Issue Detection and Monitoring of Corrosion in Steel Structures)

Abstract

:
To explore the corrosion of Q235 steel in sand containing a simulated haze aqueous solution (HA solution) under a natural air-dried state, the effect of moisture (age) on the corrosion of Q235 steel in sand was comprehensively studied by EIS, polarization curve, SEM, EDS and XPS. The physical and chemical properties of the sand showed that the sand containing the HA solution was basically neutral under natural air drying, and the temperature was around 20 °C. After 14 days, the moisture content gradually decreased from 30% to 0%, and the salinity decreased from 1.26% to 0.04%. With the increase in age, the Eocp gradually positively skews, indicating the corrosion kinetics of the Q235 steel decrease. The impedance spectra showed that in the frequency of 10−2–103 Hz, the impedance spectra exhibited a flat capacitive loop, and the corrosion of Q235 steel was the strongest in the sand containing HA solution on the 8 d. The polarization curves showed that with increasing age, the degree of corrosion of Q235 steel changed from medium or above to slight corrosion in the sand containing HA solution. The pitting characteristics of anode branch for polarization curve also indicate the faster corrosion kinetics of Q235 steel in the early age (1–5 d). The corrosion current density Io first increased and then decreased, and the highest value was 3.44 × 10−5 A/cm2 at 6 d. The average corrosion rate was 0.1629 mm/a. HA solution accelerates the corrosion of Q235 steel in sand without HA solution (average corrosion rate, 1.51 × 10−2 mm/a). A large amount of brown-yellow corrosion products (iron oxides, about 70–200 μm) presented on the surface of the Q235 steel. The corrosion of Q235 steel belonged to local corrosion, and the corrosion pits were connected to form a large dimple-like area. The HA solution and the porous structure of sand jointly affect the electrochemical corrosion of Q235 steel.

1. Introduction

Q235 steel has good plasticity, toughness and weldability and is widely used in construction and engineering structures, such as vehicles, boilers, containers, etc. In addition, before the end of the 1940s, ordinary carbon steel (Q235) was used for pipeline steel [1]. However, the corrosion resistance of Q235 steel is poor, and Q235 steel will suffer corrosion in weakly alkaline, neutral and acidic environments (including the atmosphere, water and soil), which will cause significant losses of economy, resources and energy and threaten the safety of the corresponding grounding infrastructure and personnel. The rapid development of urbanization and industrialization has led to the deterioration of the environment. “Smog weather” usually occurs in winter, but pollutants are present in the air all year round. Fine particulate matter (PM 2.5) in the atmosphere enters the soil with rain, which causes the transformation of soil quality [2,3]. Rainfall, growth absorption, water loss from terrain, and human activities all affect changes in the water content in the soil environment and subsequently affect soil corrosion. In addition, soil corrosion is affected by soil resistivity, soluble salts, water content, pH and the interactions of the factors. The factors often vary with time and space, and they are very complex [4]. Therefore, the rules and mechanism of soil corrosion still need to be further explored and studied.
Soil corrosion is one of the main causes of grounding infrastructure failure, and it is hidden and difficult to detect. Soil is a complex electrolyte system. Water provides soil with an electrolyte [5]. There are many kinds of soil in China, and the corrosion resistances of the same material in different soils are very different. Currently, natural environment corrosion test nets have been built in our country. Particles in sand have no adsorption effect on ions, and the corrosion of metal materials has certain characteristics [6]. Studying the electrochemical corrosion mechanism of Q235 steel in sand under a natural air-dried state (moisture from saturated to dry) is helpful for evaluating the corrosion status of Q235 steel through rainfall or human activities to guide engineering application.
In recent years, the corrosion of Q235 steel in soil environments with different properties [6], such as magnesium chloride polluted sandy silt soil, silt soil containing sodium chloride, sand [7], diatomite soil [8], sodium bentonite [9], bentonite clay [10] and alternating wet and dry soil [11] was studied by electrochemical testing techniques and morphological composition testing techniques. The simulated acid rain heavily increased the corrosion rate of Q235 steel in the acidic soil in Yingtan [12]. The Q235 steel in acidic soil in Singapore was mainly corroded locally and with severe corrosion [13]. The electrochemical characteristics of the sand were analyzed from the characteristics of the interfaces of the three phases, the basic model and the equivalent circuit fitting. In sandy soil (gas, liquid, solid multiphase corrosion system), the cathode distribution on the metal surface depends on the total length of the three phases boundary per unit area (Ltpb), which is an important factor affecting the corrosion behavior [14]. To further explore the influence of pore fluid on the electrochemical corrosion of Q235 steel in sand containing simulated haze aqueous solution (HA solution), the electrochemical corrosion of Q235 steel in sand under a natural air-dried state was studied based on electrochemical theory.

2. Materials and Methods

2.1. Materials

The test employed Xiamen ISO standard sand with a SiO2 content exceeding 98%. The maximum dry density (ρdmax) and minimum dry density (ρdmin) were 1.86 g/cm3 and 1.56 g/cm3, respectively. The grain size accumulation curve shows that the gradation of the sand is discontinuous, but the soil is a good grade of coarse sand, which meets the two conditions of Cu ≥ 5 and Cc = 1–3 at the same time [15]. The composition and content of the HA solution are shown in Table 1. The ratio of SO42−, NO3, NH4+ and Cl ions is 5:4:1:2 [16]. Pure water was used in this work. The representative pipeline steel Q235 was selected as the working electrode and was characterized by a low carbon content. The components are shown in Table 2. The samples were Q235 steel sheets with dimensions of Φ15 mm × 2 mm. The samples were successively polished with #360, #800 and #1500 SiC sandpapers before testing and subsequently blown dry after ultrasonic cleaning in an acetone solution for 10 min. Afterwards, a working area of 1 cm2 was left on the surface of the working electrode through wax sealing. The electrolytic cell was a rubber soil sample box with an internal volume of 70.7 × 70.7 × 70.7 mm3. The weight of the sand soil was 300 g and the initial weight of the water was 90 g. The precision of the Libra was 0.01.

2.2. Methods

The initial water content was 30% (saturated state), and the test ages were 1 d, 2 d, 3 d, …, until the sand was air-dried. The electrochemical impedance spectra and polarization curves of the Q235 steel in sand were obtained by an electrochemical workstation (CS350H, Wuhan Corrtest Instruments Corp., Ltd., Wuhan, China). A Q235 steel electrode (WE, working electrode), saturated calomel electrode SCE (RE, reference electrode) and titanium mesh (CE, counter electrode) were, respectively, the three electrodes. The open-circuit potential (OCP) was measured for 20 min. Electrochemical impedance spectra were tested under the condition of an AC amplitude of 5 mV and scanning frequency of 10−2–105 Hz. The potentiodynamic polarization test was proceeded under the parameters of a potential range of −1–2 V near the open-circuit potential and a scanning rate of 3 mV/s. The temperature, moisture, salinity and pH of the sand were tested by soil meter (FK-WSYP). The height of 300 g of sand was 3.5 cm, and the soil was loose. The working electrode was buried in sand at a depth of 2 cm. The properties test height of the sand was consistent with the height of the working electrode [15].
An optical digital microscope (Olympus DSX1000, Tokyo, Japan) was used to study the macroscopic corrosion morphology of the corrosion products. A scanning electron microscope (JSM-6510, Japan Electronics Co., Ltd., Hachioji, Japan) was used to observe the micromorphology of the corrosion products and Q235 steel at magnifications of ×50, ×100, ×200, ×500 and ×1000. An energy spectrometer (GENESIS, EDAX, Mahwah, NJ, USA) and X-ray photoelectron energy spectrometer (Thermo Scientific EscaLab Xi+, Thermo Fisher Scientific, Waltham, MA, USA) were used to test the energy dispersive spectroscopy (EDS) and X-ray photoelectron spectroscopy (XPS) of the corrosion products, respectively. The pickling solution used for cleaning rust was a 1000 mL solution consisting of 500 mL hydrochloric acid (HCl, ρ = 1.19 g/mL), 3.5 g hexamethylenetetramine and distilled water. The temperature was 20–25 °C, and the soaking time was 5–10 min.

3. Results

3.1. Properties of Sand Containing HA Solution

The physical and chemical properties of sand containing the HA solution under a natural air-dried state are shown in Table 3. The pH fluctuated in the scope of 6.34–7.01, and the sand was basically neutral. The temperature also changed by approximately 20 °C.
The sand containing the HA solution gradually dries from 30% to 0% within 14 days. The salt gradually decreased from 1.26% to 0.04% within 14 days.

3.2. Open-Circuit Potential of Q235 Steel in Sand Containing HA Solution

Figure 1 presents the open-circuit potential (Eocp) of Q235 steel in sand containing HA solution under natural air drying. It is stable with time. With the increase in age, that is, the decrease in moisture content in the sand, the Eocp of Q235 steel in sand gradually-positively skews.

3.3. Electrochemical Impedance Spectra of Q235 Steel in Sand Containing HA Solution

Figure 2 shows the Nyquist diagrams of Q235 steel in sand containing HA solution in the natural air-dried state. With the increasing age, that is, decreasing moisture content, the impedance spectra fluctuate greatly in the frequency area of 103–106 Hz after 8 days. The parts with large fluctuations are not presented and analyzed here. In the frequency area of 10−2–103 Hz, the impedance spectra present a flat capacitive loop, the intersection point with the real axis shifts to the left, and the radius of the capacitive loop decreases first and then increases.
Figure 3 is the modulus value and Figure 4 is the phase angle of Q235 steel in natural HA-containing sand. The impedance spectra are not the type of onetime constant, which is consistent with the impedance spectra. After 8 d, the impedance spectra fluctuate greatly in the frequency range of 103–106 Hz.
To further study the characteristics, the non-fluctuation part of the impedance spectra of Q235 was fitted by the equivalent circuit Re(Cs(Rs(Qdl(RctW)))) (Figure 5) according to the characteristics of the modulus and phase angle [15]. The fitting results are shown in Figure 6 and Figure 7 and Table 4, which are obtained by the fitting software ZSimDemo 3.30d. Figure 6 and Figure 7 show that the fitting effect of the equivalent circuit is good.

3.4. Polarization Curve of Q235 Steel in Sand Containing HA Liquid

Figure 8 is the polarization curves of Q235 steel in sand containing HA solution under a natural air-dried state. With the increase in age, that is, as the moisture content in the sand decreases continuously, the polarization curve shifts upward overall, and the corrosion of Q235 steel gradually weakens. During 1 d–7 d, the corrosion potential of the Q235 steel is around −1 V, and passivation of the anode branch is obvious. After 8 days, the corrosion potential gradually increased to about −0.8 V. At 1 d, a wide platform appeared in the anode branch of the polarization curve, showing a relatively stable current density, which may be related to the solid–liquid path in the initial saturation state in the sand. During 2–5 d, an activation–passivation transition zone appears in the range of −1–0 V of the anodic branch. On the one hand, the water content in the sand decreases, forming a solid–liquid–gas three-phase path; On the other hand, the pore liquid contains Cl, and the anode branch presents the characteristics of pitting. Over 1–5 d, pitting potential gradually shifts from around 0 V to about −0.5 V.
To further study the corrosion rate of Q235 steel in sand containing HA solution, the polarization curves were fitted by Rp weak polarization at ±50 mV near the open circuit potential. The results are shown in Table 5. The polarization resistance Rp decreases first and then increases, reaching a peak value at 7 d. Io is the corrosion current density. The corrosion grade of Q235 steel first increases, reaching the highest level (3.44 × 10−5 A/cm2) at 6 d, and then decreases. The corrosion potential E0 basically shifts to the negative direction.

3.5. Electrochemical Corrosion Mechanism of Q235 Steel in Sand Containing HA Solution

Figure 9 shows the macroscopic corrosion morphology of Q235 steel in sand containing HA solution under natural air-dried state, and the magnification of the picture is 18×. The results indicate that the surface of Q235 steel has highly variable brown-yellow corrosion products (iron oxides). Figure 9b shows that the thickness of the corrosion products is about 70–200 μm and the height varies. The SEM images of the corrosion products are show in Figure 10. The corrosion products were in the shape of lamellar, flocculent clusters, rice grains, etc.
The EDS and XPS analysis were further performed on the corrosion products on the Q235 selected in Figure 9. The EDS results (Table 6) indicate that the corrosion products are mainly composed of Fe, O and C. And small amounts of Na, S and Cl are present. The XPS analysis results of the corrosion products are shown in Figure 11. As shown in the full spectrum XPS scanning diagram in Figure 11a, the elements in the corrosion products mainly include Fe, O and C. The C may come from the matrix of the sample and adventitious carbon, Na may be the precipitation of sodium salts, and Fe and O may come from the surface corrosion products.
The corrosion morphology of Q235 steel was further analyzed via SEM after removing the rust. The magnifications were ×50, ×100, ×200, ×500 and ×1000 (Figure 12). The corrosion of Q235 steel is local corrosion, and corrosion pits are connected to form a large area of dimples.

4. Discussion

The Eocp of Q235 steel in sand gradually positively skews, indicating that the corrosion kinetics of Q235 steel in sandy soil decrease with the increase in age [17]. In the high-frequency region, solid, solution and gas in sand containing HA solution will all form conductive paths, and the impedance spectrum will fluctuate greatly when the water content is low [15,18]. In sandy soil, Cl has greater mobility and aggression, while SO42− has more charge. The impedance spectrum radius of Q235 steel in sand containing HA solution is smaller than that in sand without HA solution [15]. At 8 d, the water component of the sand containing the HA solution is 12.5%, which is near the limit volume content of the liquid bridge (6%–12%). The arc radius of the capacitive loop reached a minimum, and the sand had the strongest corrosion on the Q235 steel. The water content in the liquid bridge limit volume is respectively about 6% and 12% for the loose simple cube arrangement and the compact tetrahedron arrangement. When the water content is 6%–12%, the water content in the sand is near the liquid bridge limit volume. Water content continues to decrease, and there are lenticular or annular water films on the contact points of sand particles that are not connected with each other [15].
Table 4 shows that after the water component reaches less than the limit liquid bridge volume (8 d), the fitting parameters of the impedance spectra change greatly, which may be caused by the complex distribution of the pore liquid. With decreasing water in sand, the solution resistance (Re), sand layer resistance (Rs) and charge transfer resistance (Rct) increase, but the order of magnitude of Rs changes little. In addition, the order of magnitude the diffusion impedance (W) representing tortuosity fluctuates greatly, which is probably because the complex pore structure of sand containing HA solution [19]. Qdl is a constant phase element, the values of n are all less than 0.8 and the interface capacitance deviates from the ideal capacitance.
The pitting characteristics of anode branch for polarization curve also indicate the faster corrosion kinetics of Q235 steel in the early age (1–5 d) [17]. The Io of Q235 steel is above 3 μA/cm2 at 1 d–13 d, the corrosion degree of Q235 steel is above medium, the corrosion degree is below 3 μA/cm2 at 14 d and the corrosion of Q235 steel is mild [19]. The overall corrosion rate decreases gradually from 10−1 to 10−3 and the average corrosion rate is 0.1629 mm/a. HA solution accelerates the corrosion of Q235 steel in sand without HA solution (average corrosion rate, 1.51 × 10−2 mm/a). The addition of HA solution increases the corrosion rate of Q235 steel by orders of magnitude, and the corrosion potential E0 basically shifts to the negative direction, which increases the corrosion tendency [15].
The surface of Q235 steel has highly variable brown-yellow corrosion products (iron oxides, about 70–200 μm), which is closely related to the porous structure of sand containing the HA solution. The part in contact with the pore solution (HA solution) can directly carry out electrochemical corrosion, and the corresponding product presents a darker color [20]. The SEM images of the corrosion products (Figure 10) showed that the corrosion products were in the shape of lamellar, flocculent clusters, rice grains, etc.
The EDS results (Table 6) indicate that the corrosion products are mainly composed of Fe, O and C. And small amounts of Na and Cl are present. Therein, Fe and O are in compositions of brown and yellow iron oxides. In the O1s fine spectrum (Figure 11b), the peak at 529.34 eV represents the formation of iron oxides, while the peak at 530.99 eV may be caused by the coexistence of various iron oxides and adhesive sand particles (SiO2), with multiple overlapping components [21]. In the Fe2p fine spectrum (Figure 11c), the characteristic peak at 710.74 eV represents the formation of Fe2p3/2(Fe2O3), and the peak at 724.14 eV represents the formation of Fe2p1/2(Fe2O3) [22]. In the Na1s fine spectrum (Figure 11d), the peaks at 1071–1071.5 eV represent sodium compounds. In the C1s fine spectrum (Figure 11e), the peak at 284.8 eV represents the chemical state of C-C, while the peak at 288.46 eV represents the chemical state of O-C=O. On the one hand, the metal matrix is an iron–carbon alloy, and on the other hand, adventitious carbon is adsorbed on the sample [23].
Fe2O3 is the main component of the corrosion products. Anode dissolution will produce Fe2+, which may react with H2O in the neutral pore liquid to form Fe(OH)2 (Formula (3)) and further oxidize to form Fe2O3 on the Q235 steel [24,25]. When the steel is in contact with the sand, a circuit is formed through the sand to form a corrosion battery, and an electrochemical reaction can occur.
F e 2 e F e 2 +
O 2 + 4 H + + 4 e 2 H 2 O
F e 2 + + 2 H 2 O F e ( O H ) 2 + 2 H +
4 F e ( O H ) 2 + O 2 2 F e 2 O 3 + 4 H 2 O
F e + 2 C l F e C l 2 + 2 e
2 H 2 O + 4 e + 4 N a + + O 2 4 N a O H
F e C l 2 + N a O H + O 2 F e 2 O 3 · H 2 O + N a C l + H 2 O
2 F e S O 4 + O 2 + H 2 O F e 2 O 3 · H 2 O + H 2 S O 4
The HA solution and porous structure of sand affect the electrochemical corrosion of Q235 steel, and Figure 12 shows that HA solution strongly aggravates the corrosion of Q235 steel in sand [15].

5. Conclusions

Based on electrochemical theory and the corrosion principle of Q235 steel, the electrochemical corrosion of Q235 steel in sand containing HA solution under a natural air-dried state was comprehensively studied. The following conclusions are obtained:
(1)
The pH of the sand containing the HA solution fluctuated within the range of 6.31–7.01, the sand was basically neutral and the temperature changed by around 20 °C. The moisture gradually decreased from 30% to 0%, and the salt decreased from 1.26% to 0.04% within 14 days;
(2)
The Eocp of Q235 steel is stable with time. With the increase in age, the Eocp gradually-positively skews indicating the corrosion kinetics of Q235 steel in sandy soil decrease. In the frequency of 10−2–103 Hz, the impedance spectra present a flat capacitive loop. The water component of the sand is near the limit volume content of the liquid bridge (6%–12%) at 8 d. The radius of capacitive loop is the smallest, and sand erodes steel the most. After 8 d, the impedance spectra fluctuate greatly in the frequency of 103–106 Hz;
(3)
As age increases, the polarization curve of Q235 steel moves upward overall, and the corrosion tendency of Q235 steel in sand containing HA solution gradually weakens. The pitting characteristics of the anode branch for polarization curve also indicate the faster corrosion kinetics of Q235 steel in the early age (1–5 d). The corrosion grade of Q235 steel first increases and then decreases, reaching the highest level (3.44 × 10−5 A/cm2) at 6 d. The corrosion degree of Q235 steel varies from medium to mild corrosion. The average corrosion rate is 0.1629 mm/a. HA solution accelerates the corrosion of Q235 steel in sand without HA solution (average corrosion rate, 1.51 × 10−2 mm/a).
(4)
The surface of the Q235 steel was stacked with highly different brown–yellow corrosion products (iron oxides, about 70–200 μm), and the corrosion products were lamellar, flocculent clusters, rice grains and other shapes. The corrosion of the Q235 steel was local corrosion, and corrosion pits connected to form a large area of dimples. The HA solution and porous structure in sand jointly affect the electrochemical corrosion of Q235 steel.

Author Contributions

Writing—original draft, R.X., Y.B., R.G., Q.Z., H.H., Y.W., B.L., P.H., Z.W., S.W., N.L. and B.D. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by PhD research launch project of Jinzhong University (No. jzxybsjjxm2019019), “1331” Innovation Team of Jinzhong University (No. jzxycxtd2019008), National Natural Science Foundation of Shanxi Province (No. 202103021224306, No. 20210302123139), Shanxi Collaborative Innovation Center for Lightweight Material Modification and Application and Shanxi Province Science and Technology Innovation Young Talents Team (No. 202204051001005). Opening Project of Sichuan University of Science and Engineering, Material Corrosion and Protection Key Laboratory of Sichuan province (No. 2020CL13, No. 2021CL22).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

All the data used to support the findings of this study are present in the paper.

Conflicts of Interest

The authors declare no conflicts of interest.

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Figure 1. Open circuit potential of Q235 steel in sand containing HA solution: 1–14 d.
Figure 1. Open circuit potential of Q235 steel in sand containing HA solution: 1–14 d.
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Figure 2. Nyquist diagram of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
Figure 2. Nyquist diagram of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
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Figure 3. Modulus of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
Figure 3. Modulus of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
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Figure 4. Phase angle of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
Figure 4. Phase angle of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
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Figure 5. Equivalent circuit model of sand-steel interface.
Figure 5. Equivalent circuit model of sand-steel interface.
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Figure 6. Equivalent circuit fitting results of the impedance spectra of Q235 steel in sand containing HA solution (1 d–7 d).
Figure 6. Equivalent circuit fitting results of the impedance spectra of Q235 steel in sand containing HA solution (1 d–7 d).
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Figure 7. Equivalent circuit fitting results of the impedance spectra of Q235 steel in sand containing HA solution (8 d–14 d).
Figure 7. Equivalent circuit fitting results of the impedance spectra of Q235 steel in sand containing HA solution (8 d–14 d).
Coatings 14 00491 g007
Figure 8. Polarization curves of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
Figure 8. Polarization curves of Q235 steel in sand containing HA solution: (a) 1 d–7 d; (b) 8 d–14 d.
Coatings 14 00491 g008
Figure 9. Macroscopic corrosion morphology of Q235 steel in sand containing HA solution: (a) 2D image; (b) 3D image (The area in the red circle will be further analyzed by EDS and XPS).
Figure 9. Macroscopic corrosion morphology of Q235 steel in sand containing HA solution: (a) 2D image; (b) 3D image (The area in the red circle will be further analyzed by EDS and XPS).
Coatings 14 00491 g009
Figure 10. SEM images of corrosion products on the surface of Q235 steel in sand containing HA solution: (a) ×50; (b) ×100; (c) ×200; (d) ×500; (e) ×1000.
Figure 10. SEM images of corrosion products on the surface of Q235 steel in sand containing HA solution: (a) ×50; (b) ×100; (c) ×200; (d) ×500; (e) ×1000.
Coatings 14 00491 g010
Figure 11. XPS of the corrosion products on Q235 steel: (a) full spectrum and elemental chemical bond analysis: (b) O1s fine spectrum; (c) Fe2p fine spectrum; (d) Na1s fine spectrum; (e) C1s fine spectrum.
Figure 11. XPS of the corrosion products on Q235 steel: (a) full spectrum and elemental chemical bond analysis: (b) O1s fine spectrum; (c) Fe2p fine spectrum; (d) Na1s fine spectrum; (e) C1s fine spectrum.
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Figure 12. Microscopic corrosion morphology of Q235 steel in sand containing HA solution after rust cleaning: (a) ×50; (b) ×100; (c) ×200; (d) ×500; (e) ×1000.
Figure 12. Microscopic corrosion morphology of Q235 steel in sand containing HA solution after rust cleaning: (a) ×50; (b) ×100; (c) ×200; (d) ×500; (e) ×1000.
Coatings 14 00491 g012
Table 1. Composition and content of the simulated haze aqueous solution (HA solution).
Table 1. Composition and content of the simulated haze aqueous solution (HA solution).
CompositionNa2SO4NaNO3NH4ClNaClH2O
Content (mol·L−1)0.050.040.010.01BAL.
Table 2. Chemical composition of Q235 steel (wt.%).
Table 2. Chemical composition of Q235 steel (wt.%).
CompositionCSiMnPSFe
Content (wt.%)0.220.480.010.220.022Bal.
Table 3. Physical and chemical properties of sand containing HA solution.
Table 3. Physical and chemical properties of sand containing HA solution.
Age (d)Salt Content (%)pHWater Component (%)Temperature (°C)
11.266.5530.021.8
21.146.3426.021.4
31.066.6119.020.5
40.796.6818.819.2
50.886.6317.519.3
60.596.7015.919.9
70.636.6414.421.5
80.436.9912.518.7
90.316.8511.319.4
100.196.928.520.3
110.126.966.218.6
120.047.013.419.4
130.046.880.519.0
140.046.940.021.9
Table 4. Equivalent circuit fitting results of the impedance spectra of Q235 steel in sand containing HA solution.
Table 4. Equivalent circuit fitting results of the impedance spectra of Q235 steel in sand containing HA solution.
Age (d)Re (Ω·cm2)Cs (F·cm−2)Rs (Ω·cm2)QdlRct (Ω·cm2)W (S·s0.5·cm−2)
Yo (S·s−n·cm−2)n
11.26 × 1021.55 × 10−86.50 × 1011.99 × 10−40.84 2.36 × 1031.56 × 1010
21.08 × 1021.26 × 10−86.91 × 1017.79 × 10−40.65 2.09 × 1034.20 × 108
31.08 × 1021.33 × 10−91.09 × 1025.85 × 10−40.72 1.63 × 1031.56 × 10−3
41.07 × 1023.43 × 10−97.00 × 1017.01 × 10−40.71 1.42 × 1031.19 × 10−2
51.12 × 1023.51 × 10−97.60 × 1011.73 × 10−30.57 1.51 × 1037.58 × 10−3
61.19 × 1022.84 × 10−98.84 × 1013.05 × 10−30.49 2.83 × 1036.02 × 10−3
71.91 × 1021.22 × 10−91.78 × 1024.30 × 10−30.41 1.98 × 1031.02 × 103
88.37 × 1028.63 × 10−101.93 × 1032.35 × 10−30.40 7.42 × 1026.13 × 107
96.68 × 1029.43 × 10−102.96 × 1031.27 × 10−30.61 5.34 × 1024.84 × 10−2
103.35 × 1035.87 × 10−83.53 × 1021.56 × 10−30.60 4.62 × 1024.28 × 10−2
111.16 × 1024.61 × 10−93.72 × 1045.19 × 10−70.51 2.09 × 1053.90 × 10−5
123.16 × 1021.03 × 10−95.09 × 1033.24 × 10−30.20 4.07 × 1035.72 × 108
136.64 × 1027.76 × 10−84.24 × 1024.27 × 10−30.61 2.44 × 1021.93 × 10−2
149.43 × 1039.23 × 10−134.52 × 1037.76 × 10−60.41 7.18 × 1045.88 × 10−4
Table 5. Rp fitting results of the polarization curves of Q235 steel in sand containing HA solution.
Table 5. Rp fitting results of the polarization curves of Q235 steel in sand containing HA solution.
Age (d)Corrosion Rate (mm/a)Rp (Ω/cm2)Io (A/cm2)Eo (V)
11.10 × 10−12.59 × 1031.01 × 10−5−0.95
21.50 × 10−11.92 × 1031.36 × 10−5−0.98
31.80 × 10−11.69 × 1031.55 × 10−5−0.99
42.40 × 10−11.24 × 1032.11 × 10−5−1.00
53.30 × 10−19.23 × 1022.83 × 10−5−0.99
64.00 × 10−17.59 × 1023.44 × 10−5−0.99
73.90 × 10−17.74 × 1023.37 × 10−5−0.93
81.17 × 10−12.62 × 1039.95 × 10−6−0.72
91.05 × 10−12.93 × 1038.90 × 10−6−0.71
107.53 × 10−24.08 × 1036.40 × 10−6−0.74
116.65 × 10−24.61 × 1035.65 × 10−6−0.72
125.13 × 10−25.98 × 1034.36 × 10−6−0.68
136.01 × 10−25.11 × 1035.11 × 10−6−0.69
145.97 × 10−35.14 × 1045.08 × 10−7−0.64
Table 6. Elemental content analysis (EDS) of corrosion products for different selections: (a) all selection; (b) protrusion region; (c) flat region.
Table 6. Elemental content analysis (EDS) of corrosion products for different selections: (a) all selection; (b) protrusion region; (c) flat region.
SectionElementCKOKNaKSiKSKClKMnKFeKMatrix
Coatings 14 00491 i001Wt%5.6914.223.500.341.401.000.6273.24Correction
At%16.2130.425.210.411.490.970.3944.90ZAF
Coatings 14 00491 i002Wt%5.4621.903.120.142.331.660.4464.95Correction
At%13.9642.064.170.152.241.440.2535.74ZAF
Coatings 14 00491 i003Wt%5.8914.852.200.350.831.120.4474.31Correction
At%16.7831.753.270.430.891.080.2745.52ZAF
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MDPI and ACS Style

Xie, R.; Bao, Y.; Geng, R.; Zhang, Q.; Hou, H.; Wang, Y.; Li, B.; Han, P.; Wang, Z.; Wang, S.; et al. Study on Electrochemical Corrosion of Q235 Steel in Sand Containing HA Solution under a Natural Air-Dried State. Coatings 2024, 14, 491. https://doi.org/10.3390/coatings14040491

AMA Style

Xie R, Bao Y, Geng R, Zhang Q, Hou H, Wang Y, Li B, Han P, Wang Z, Wang S, et al. Study on Electrochemical Corrosion of Q235 Steel in Sand Containing HA Solution under a Natural Air-Dried State. Coatings. 2024; 14(4):491. https://doi.org/10.3390/coatings14040491

Chicago/Turabian Style

Xie, Ruizhen, Yage Bao, Ruicheng Geng, Qi Zhang, Haosheng Hou, Yakang Wang, Boqiong Li, Pengju Han, Zhenxia Wang, Shiying Wang, and et al. 2024. "Study on Electrochemical Corrosion of Q235 Steel in Sand Containing HA Solution under a Natural Air-Dried State" Coatings 14, no. 4: 491. https://doi.org/10.3390/coatings14040491

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