Hongyang Weia,
Dongchu Chen*a,
Huawen Hu*a,
Menglei Changa,
Xiufang Yea and
Meifeng Wangb
aSchool of Material Science and Energy Engineering, Foshan University, Foshan 528000, Guangdong, China. E-mail: cdcever@163.com; huawenhu@126.com
bSchool of Material Science and Engineering, Nanchang Hangkong University, Nanchang 330063, China
First published on 8th December 2017
In this study, the impact of various sealing conditions on the quality of the sealed anodic aluminum oxide (AAO) film is systematically investigated, which leads us to gain insights into sealing the AAO film. To this end, magnesium acetate and calcium acetate are employed as the main compositions of the sealant. It is demonstrated that the temperature exerts the greatest influence on the quality of the sealed film based on the weight loss and antistaining adsorption evaluations among the other examined conditions, followed by pH, mixed salts, surfactants, and complexants. For the optimized sample, the minima of the staining level and weight-loss ratio can reach 0 and 13.4 mg dm−2, respectively, meeting the requirement of the ISO standard. This work also realizes an energy-efficient sealing of the AAO film at intermediate temperatures (75–85 °C). The potentiodynamic scanning and electrochemical impedance spectroscopy measurements reveal that the AAO film sealed by the alkaline earth metal salt possesses a superior corrosion resistance as compared to the one sealed by the conventional nickel salt. Additionally, the potential can be stable in a faster way at higher temperatures over the range of 70–85 °C, as demonstrated in the E–t curve. On the other hand, the potential stabilization is more readily achieved at higher pH values within the range of 5–7, whereas it cannot be realized at pH values above 7. We also note that the appropriate addition of surfactant, complexant and pH buffer can assist in stabilizing the potential. In the absence of any surfactants and complexants, the potential stabilization cannot be reached. Furthermore, the present study discusses the mechanism underlying the effective sealing, thereby paving the way for the future exploration of the energy-efficient and eco-friendly sealing technologies for many practical AAO-based applications.
In these regards, there is a pressing need to develop an energy-efficient, eco-friendly, and highly corrosion-resistant sealing method. Actually, many attempts have been made to fill the micropores of the AAO film using different kinds of rare earth compositions by immersing the rare earth metal salts into the anodic oxidation solution,7 but such a direct immersion is not able to incorporate the rare earth metal compositions into the interior of the AAO film pores.7b Alternatively, hole sealing of the AAO film is also realized by chemical treatment and electrochemical deposition processing of the porous structure.8 Nevertheless, only a mediocre sealing quality and hence a moderate corrosion resistance can be usually obtained, indicating that further efforts are required to improve the sealing quality relative to that achieved by many conventional sealing methods.
The hole sealing of AAO films based on alkaline earth metal salts lies in using alkaline metal salts or alkaline earth metal salts as the main compositions of the sealant. Such a sealing method is environmentally friendly and cost-efficient. A number of studies have been reported on the hole sealing of AAO films based on alkaline earth metal salts,1c,d,6b but the sealing mechanism has not been explored by far, with the focus primarily on obtaining high-quality sealed AAO films. Therefore, in this study, magnesium acetate and calcium acetate are adopted as the main composition of the sealant for sealing the holes of the AAO film. The sealing condition is systematically investigated, so as to unravel the mechanism underlying the effective sealing of the AAO film. The sealing quality is evaluated on the basis of the antistaining adsorption and weight loss tests. Not only does this study find the best conditions for high-quality sealing of the AAO film, but it also puts forward the mechanism underlying the effective sealing.
Fig. 2 Evaluation of the sealing quality for various samples based on the antistaining adsorption (a) and weight loss test (b). |
Apart from the antistaining adsorption evaluation, this study also adopted the weight loss test to further evaluate the sealing quality of the samples 1–16, with the results given in Fig. 2b. According to the ISO3210:19835 standard, the samples with the weight loss of below 30 mg dm−2 are qualified. It can be noted that the samples 4, 5, 6, 9, 11, and 16 exhibit a weight loss smaller than 30 mg dm−2, revealing a qualified sealing. The remaining samples have an excessive weight loss, implying a poor anticorrosion performance and a low sealing quality. For the samples 4, 5, 6, 9, 11, and 16, the weight loss values are estimated as 19.2, 13.4, 23.4, 29.4, 13.5 and 28.9 mg dm−2, respectively. The smaller the weight loss value, the higher the sealing quality. The samples 4, 5, 6, 9, 11 and 16 also possess the satisfactory staining level of 0 or 1 (Fig. 2a), thus indicating that weight loss test results are in great consistence with that of the antistaining adsorption test. In this study, the influence of various hole sealing conditions is also systematically investigated through the weight lost test, including the concentrations of the salt mixture, complexant and surfactant, and pH and temperature, as shown in Fig. 3. The variance analysis of the weight loss index is also done (see Table 2).
Sample code | Conc. of the salt mixture (g L−1) | Conc. of the complexing agent (g L−1) | Conc. of the surfactant (g L−1) | pH | T (°C) |
---|---|---|---|---|---|
1 | 2.5 | 10 | 0.25 | 5.0 | 70 |
2 | 2.5 | 13 | 0.5 | 6.0 | 75 |
3 | 2.5 | 16 | 0.75 | 7.0 | 80 |
4 | 2.5 | 19 | 1 | 8.0 | 85 |
5 | 5 | 10 | 0.5 | 7.0 | 85 |
6 | 5 | 13 | 0.25 | 8.0 | 80 |
7 | 5 | 16 | 1 | 5.0 | 75 |
8 | 5 | 19 | 0.75 | 6.0 | 70 |
9 | 7.5 | 10 | 0.75 | 8.0 | 75 |
10 | 7.5 | 13 | 1 | 7.0 | 70 |
11 | 7.5 | 16 | 0.25 | 6.0 | 85 |
12 | 7.5 | 19 | 0.5 | 5.0 | 80 |
13 | 10 | 10 | 1 | 6.0 | 80 |
14 | 10 | 13 | 0.75 | 5.0 | 85 |
15 | 10 | 16 | 0.5 | 8.0 | 70 |
16 | 10 | 19 | 0.25 | 7.0 | 75 |
Factor | Square of deviance | Degree of freedom | F ratio | F0.05 critical value | F0.10 critical value |
---|---|---|---|---|---|
Mixed salt | 5497.085 | 3 | 0.176 | 9.280 | 5.390 |
Complexing agent | 1588.895 | 3 | 0.051 | 9.280 | 5.390 |
Surfactant | 2620.265 | 3 | 0.084 | 9.280 | 5.390 |
pH | 12859.470 | 3 | 0.412 | 9.280 | 5.390 |
Temperature | 31238.265 | 3 | 1.000 | 9.280 | 5.390 |
Error | 53803.98 | 15 | — | — | — |
From Fig. 3, it can be noted that the weight loss is initially increased and then decreased with raising the contents of the mixed salts; the lowest weight loss value is found at the 10 g L−1 content. The weight loss value is lowered first and becomes increased with the increase of the complexant content; the minimum value of the weight loss can be noted at 16 g L−1. For the impact of the surfactant, the weight loss mean value is initially lowered and consequently raised as the content of the surfactant increases, with the lowest weight loss value at 0.5 g L−1. Concerning pH influence, the weight loss value is decreased first and become raised as the pH rises, with the smallest weight loss value found at pH 7. The temperature linearly affects the weight loss values; the higher the temperature, the smaller the weight loss value. The minimum value of the weight loss is achieved at 85 °C. The optimized formulation and technological conditions are given as follows: 10 g L−1 mixed salts (Ca(CH3COO)2·H2O, C4H6O4Mg·4H2O), 16 g L−1 complexant (C6H15NO3), 0.5 g L−1 surfactant (C24H32O7S2Na2), 2 g L−1 pH buffer (CH3COONH4), and at pH 7 and 85 °C. The variance analysis, as shown Table 2, reveals that the order of significance of experimental conditions on the basis of weight loss test of the sealed samples is given as follows: temperature > pH > conc. of mixed salts > conc. of surfactant > conc. of complexant.
Hole sealing mode | Electrochemical parameters | |||
---|---|---|---|---|
Ecorr (V) | Icorr (A cm−2) | Bc (mV) | Ba (mV) | |
Sealed by nickel salt | −1.2098 | 2.6171 × 10−9 | 369.94 | 567.33 |
Sealed by alkaline earth salt | −1.0720 | 1.9788 × 10−9 | 345.76 | 507.65 |
From Fig. 5(a and b), it is clear that the EIS spectra of the sealed samples are primarily composed of high-frequency and low-frequency capacitive loops. The part in the intermediate to high frequency range can reflect the main properties of the porous layer the AAO film, while the part at low frequencies can be a reflection of the main properties of the barrier layer. Based on the equivalent circuit shown in Fig. S2 of the ESI,† the Nyquist plots presented in Fig. 5(a and b) are fitted, where R1, CPE1, R2, CPE2 and CPE3 are the electric resistance of the electrolyte, capacitance and resistance of the pore wall of the porous layer, resistance of the barrier layer, and capacitance of the pore wall of the porous layer, respectively. Note that the resistance of the barrier layer was not considered in the present EIS test, which is due to the extreme big value of the fitted resistance, which can reach as high as 1021 and hence suggests the insulating state of the barrier layer. As a result, the CPE2 and CPE3 play the main role in circuit connection. From Fig. 5a, it can be noted that the capacitive loops at high frequencies are gradually expanded over time, while those at low frequencies are almost unchanged. Such a tendency can be more clearly noticed through the frequency-|Z| patterns shown in Fig. 5c. These results reveal that the porous layer of the AAO film reacts with the NaCl solution, but there is no reaction at the barrier layer. On the other hand, the capacitive loops are expanded as well at high frequencies over time as for the samples sealed by alkaline earth metal salt, together with the almost unchanged capacitive loops at low frequencies. The frequency-|Z| patterns given in Fig. 5d further clarify such a tendency. These results are a good indication of the reaction between the porous layer of the AAO film and the NaCl solution. Nevertheless, corrosion does not take place because the part at low frequencies is basically unchanged; the barrier layer does not contact with the NaCl solution. To conclude, within the socking time, the NaCl solution only interacts with the sealed porous layer, but does not etch off it, thus suggesting that it actually does not contact with the barrier layer.
Tables 4 and 5 present the electrochemical parameters related to the equivalent circuit. CPE-T and CPE-P represent capacitance and similarity level (a dimensionless constant) against CPE. It can be found that CPE1-T and CPE3-T are varied to a small extent, while the values of the CPE1-P and CPE3-P increase constantly, indicating the growing divergence from the “pure capacitance”. The resistance R2 of the porous layer is a critical index to reflect the sealing quality of the porous layer. Generally, the higher the resistance of the inner pores of the porous layer, the lower the conductivity of the porous layer; this is corresponding to the better sealing effect. The resistance of the porous layer is lowered with socking time (Table 4). Importantly, in each time period, the measured resistance R2 as for alkaline earth metal salt-sealed sample is higher than that for nickel salt-sealed one, indicating the superior corrosion resistance of the former; this is in good agreement with the potentiodynamic scanning result.
Soaking time | Samples sealed by alkaline earth salt | Samples sealed by nickel salt | ||||
---|---|---|---|---|---|---|
R2/(Ω·cm2) | CPE1-T/(F) | CPE1-P | R2/(Ω·cm2) | CPE1-T/(F) | CPE1-P | |
6 h | 824830 | 6.44 × 10−8 | 0.38743 | 275000 | 1.73 × 10−6 | 0.29500 |
3 d | 633780 | 5.74 × 10−7 | 0.39763 | 275000 | 2.29 × 10−6 | 0.28541 |
7 d | 590520 | 1.38 × 10−7 | 0.49829 | 252000 | 2.53 × 10−6 | 0.31872 |
13 d | 535900 | 2.19 × 10−8 | 0.66393 | 160000 | 4.53 × 10−7 | 0.47940 |
18 d | 289000 | 1.60 × 10−8 | 0.68831 | 130000 | 2.08 × 10−7 | 0.52639 |
24 d | 221550 | 1.52 × 10−8 | 0.69906 | 84417 | 1.30 × 10−7 | 0.55648 |
30 d | 190730 | 1.08 × 10−8 | 0.72716 | 46253 | 5.92 × 10−7 | 0.61983 |
Soaking time | Samples sealed by alkaline earth salt | Samples sealed by nickel salt | ||||||
---|---|---|---|---|---|---|---|---|
CPE2-T/(F−1) | CPE2-P | CPE3-T/(F) | CPE3-P | CPE2-T/(F) | CPE2-P | CPE3-T/(F) | CPE3-P | |
6 h | 5.80 × 10−7 | 0.93794 | 1.59 × 10−11 | 1.160 | 5.91 × 10−7 | 0.95700 | 1.05 × 10−11 | 1.132 |
3 d | 5.25 × 10−7 | 0.96737 | 9.83 × 10−11 | 1.251 | 5.49 × 10−7 | 0.97500 | 1.44 × 10−11 | 1.163 |
7 d | 5.13 × 10−7 | 0.95009 | 3.28 × 10−11 | 1.312 | 5.55 × 10−7 | 0.96701 | 3.90 × 10−11 | 1.207 |
13 d | 4.68 × 10−7 | 0.91545 | 7.36 × 10−12 | 1.388 | 5.36 × 10−7 | 0.94882 | 4.97 × 10−11 | 1.300 |
18 d | 4.58 × 10−7 | 0.91438 | 6.59 × 10−12 | 1.394 | 5.29 × 10−7 | 0.94400 | 3.41 × 10−11 | 1.321 |
24 d | 4.68 × 10−7 | 0.91549 | 5.47 × 10−12 | 1.400 | 5.16 × 10−7 | 0.96600 | 3.02 × 10−11 | 1.316 |
30 d | 4.43 × 10−7 | 0.90303 | 4.13 × 10−12 | 1.424 | 5.03 × 10−7 | 0.95300 | 1.90 × 10−11 | 1.352 |
Fig. 6 SEM images of the samples before and after hole sealing ((a) unsealed sample; (b) sealed by nickel salt; (c, d) sealed by alkaline earth metal salt). |
Fig. 7 (a) FTIR spectra of the AAO samples before and after sealing by alkaline earth metal salt. (b) EDX spectrum of the sample sealed by alkaline earth metal salt. |
Fig. 8 Investigation of various sealing conditions on E–t curves, including sealing temperature (a), surfactant (b), complexant (c), buffer solution (d) and pH (e) conditions. |
As shown in Fig. 8a, the potentials of the sealing processes at 70, 75, 80 and 85 °C come to a steady state near 1300, 1120, 1000, and 720 s. The higher the sealing temperature, the shorter the time to reach a stable potential during the sealing process. This can be due to the temperature-induced enhancement of the transfer and diffusion of various ions including Ca2+, Mg2+, and CH3COO−, etc. This reveals that increasing the temperature can drive more ions and compound molecules into the pores of the AAO film. On the other hand, the water ionization is an endothermic process, which indicates that the higher temperature facilitates the ionization of H2O and hence generates more H+. The combination of a quantity of H+ ions with the atom N of the N(CH2CH2OH)3 molecules, which possesses the un-bonded electron pairs, leaving rich OH− ions in the interior of the pores. In addition, the hydrolysis of the CH3COO− is also endothermic, suggesting that the higher temperatures facilitate the CH3COO− hydrolysis and hence increase the concentration of OH− ions. Therefore, the higher the temperature, the higher the concentration of OH− ions, along with the higher probability of the combination with Ca2+ and Mg2+ ions to form deposits. The higher rate of sealing the AAO film can hence be obtained. It can also be found that the potential for the hole sealing comes to a stabilization state in the first place at higher temperatures (Fig. 8a).
The potential of the sample sealed in the presence of the surfactant fluctuates greatly over the time period of 0–600 s, followed by a stabilization state at 1800 s (but still with a rising tendency). In contrast, the potential of the sample sealed in the presence of the surfactant becomes stable around 720 s. This indicates that the addition of the surfactant can enable the sealing process to be more quickly stabilized, facilitating the sealing of the AAO film. The surfactant C24H32O7S2Na2 possesses the excellent resistance to hard water and can form chelate compounds with Ca2+ and Mg2+, reducing the probability of forming the deposits as a result of the reaction between Ca2+ and Mg2+ metal ions and OH− ions in the solution. This can thereby soften the water. On the other hand, there are two negative charges on the C24H32O7S2Na2 molecules, which improve its solubility in the electrolyte solutions. Such a strong dispersion power of C24H32O7S2Na2 molecules can render Ca2+ and Mg2+ ions dispersive, reducing their aggregations on the surface of the AAO film and hence avoiding the generation of the deposits on the AAO surface resulting from the Ca2+ and Mg2+ ions. The AAO surface can thus be refrained from dusting. By contrast, the OH− ions, as accumulated in the solution without the surfactant, progressively react with Ca2+ and Mg2+ ions. The deposits can be formed both in the bulk solution and on the surface of the AAO film in the fashion of accumulation. It can also be noted in Fig. 8b that it is rather difficult for stabilizing the potential.
For the sealing solution with the surfactant C24H32O7S2Na2, a stable E–t curve can be obtained in a faster way, along with an effective sealing of the AAO film. The vast majority of such surfactant molecules, with the molecular weight of 542, dissociates in the bulk solution and on the external surface of the AAO film. Only a trace amount of the surfactant molecules can enter the 10–20 nm-sized micropores of the AAO film. Assuming the spherical model of the surfactant C24H32O7S2Na2 molecules, the diameter of the spheres can be calculated according to eqn (1):
(1) |
Based on the calculation, the diameter of the spherical model of the C24H32O7S2Na2 molecules can reach approximately 11.40 Å. In the bulk solution, the molecular diameters of H2O, N(CH2CH2OH)3, CH3COO−, OH−, and NH4+, Ca2+, and Mg2+ are estimated as 3.85, 7.49, 5.66, 2.37, 1.43, 1.00 and 0.89 Å, respectively. Actually, a long-chain model can be assigned to the C24H32O7S2Na2 molecules, and their molecular diameter is thus greater than 11.40 Å, especially considering their hydration state in the aqueous solution. Consequently, the highest number of the C24H32O7S2Na2 molecules, capable of simultaneously entering the micropores of the AAO film, can be estimated to be as high as 6–13, provided that the velocity of migration of the molecules into the AAO film is the same as that of the ions in the solution. The completely homogenous dispersion of C24H32O7S2Na2 molecules (0.5 g L−1) indicates that migration of each 10 nm into the 20 nm-sized pores of the AAO film corresponds to the number of the C24H32O7S2Na2 molecules of 3.4 or less (most of them forms chelate compounds with Ca2+ and Mg2+). When the AAO film is just immersed into the solution, the molecules in the bulk solution diffuses into the micropores of the AAO film. Due to a higher molecular weight of C24H32O7S2Na2, the diffusion is slow, revealing that the other smaller molecules can initially diffuse into the pores. The concentration of the C24H32O7S2Na2 molecules strikes a balance between inside and outside of the pores of the AAO film, resulting in the cease of the diffusion. After chelated with C24H32O7S2Na2 molecules in a trace amount, the Ca2+ and Mg2+ cannot affect their combination with OH− ions. The process of diffusing the surfactant molecules and various ions and molecules is illustrated by steps (I), (II) and (III) (see Scheme 1), where the C24H32O7S2Na2 molecules are corresponding to the blue spheres, and the remaining molecules and ions are also indicated by using other colored spheres. The diffusion starts in the step (I); small molecules and ions arrives at the pores of the AAO film in the step (II); the solute concentration reaches a balanced state between inside and outside of the pores of the AAO film, and then the diffusion stops in the step (III).
It can be noted that the A–B region of the E–t curve is indexed to the migration of the ions into the AAO film in the bulk solution. Over such a region, no deposits appear in the pores of the AAO film. The status of the pores of the AAO film is displayed in Scheme 1a. Owing to the conditions without involving external stirring, there exists no forced convection, revealing that such a process is controlled by the diffusion-related mass transfer. The concentration difference (or concentration gradient) between the inside and outside of the AAO film can be regarded as the impetus for the mass transfer. According to the diffusion kinetics, the existence of the convection at a certain strength is a requirement for realizing the stable diffusion. Consequently, the ion diffusion in such a process can be regarded as the unstable diffusion process. Assuming that the ion concentration is designated as c, the relationship between the distance (from outside to inside of the pores of the AAO film) and diffuse time satisfy the Fick's second law as described by using eqn (2).
(2) |
Over the B–C region, the E–t curve rises constantly, corresponding to the period of accumulating the nano-deposits in the micropores of the AAO film. In the presence of a trace amount of C24H32O7S2Na2, it is insufficient for chelating the Ca2+ and Mg2+ at a high concentration, facilitating the interactions between these alkaline metal ions and OH− at a certain concentration and hence forming deposit particles that can fill the film pores. The reactions involved in the sealing process are proposed as eqn (3)–(12).
(3) |
(4) |
CH3COO− + H2O = CH3COOH + OH− | (5) |
(CH2CH2OH)3N + H2O = H(CH2CH2OH)3N+ + OH− | (6) |
3(CH2CH2OH)3N + Al3+ = Al(CH2CH2O)3N + 3H+ | (7) |
6CH3COO− + Al3+ = Al(CH3COO)63− | (8) |
2Al(OH)3 + Al(CH3COO)63− = Al3(OH)3(CH3COO)6 + 3OH− | (9) |
NH4+ + OH− = NH3·H2O | (10) |
Ca2+ + 2OH− = Ca(OH)2↓ | (11) |
Mg2+ + 2OH− = Mg(OH)2↓ | (12) |
In such a process, the chelating reactions as illustrated in eqn (3) and (4) mainly occurs in the bulk solution, which is the reasons for observing the phenomenon that the turbid solution cannot be seen when a certain concentration of OH− ions exists in the bulk solution. The eqn (5) and (6) can basically elucidate the increase of the OH− concentration. When the concentration of the OH− ions in the pores of the AAO film arrives at a certain point, the deposits can be formed from the reactions between the OH− ions and Ca2+ and Mg2+ ions. The deposits accumulate on the inner wall of the pores of AAO film. The eqn (7) reflects the shielding effect of triethanolamine on the Al3+ ions, weakening their impact on the Ca2+ and Mg2+-based deposits. The interactions between Al3+ and CH3COO− can be displayed by eqn (8) and (9). The NH4+ ions given in eqn (8) stems from the pH buffer and has a buffering function to the rise of the concentration of OH− ions in the both the bulk solution and pores of the AAO films. This can thus mitigate the pH ascending velocity, but cannot inhibit the pH increase, helping to improve the quality of the deposits precipitated in the pores of the AAO film. The growth of the deposits in the pores of the AAO films is illustrated in Scheme 1(a–d), where the purple portion of the cross-section corresponds to the deposits. With consuming the Ca2+ and Mg2+ ions in the pores of the AAO film, a concentration difference is gradually generated between the solution concentration and bulk solution of the pores of the AAO film, facilitating the continuous diffusion of the bulk solution into the film pores. The precipitation takes place along with the diffusion, until the concentration of the C24H32O7S2Na2 molecules reach a point that can adequately chelate Ca2+ and Mg2+ ions in the film pores. At such a point, the formation of the deposits stop; in the meanwhile, the reaction also ceases. The ceasing point on the E–t curve is corresponding to the point C, together with the potential in a steady state. The C–D region of the E–t curve keeps stable, with a complete sealing sate and a basically constant electrical resistance of the AAO layer. The distribution of the deposits in the film pores in the C–D region can be partly in the state as illustrated in Scheme 1(d), while the other part being in the state as depicted in Scheme 1(c). This can be well evidenced by the SEM observation as shown in Fig. 6c. In the state illustrated in Scheme 1(d), the film pores are completely filled by the deposits, indicating that the film pores can be fully filled before the C24H32O7S2Na2 reaches a certain concentration in the film pores. For the state indexed to the film pores being not fully filled (Scheme 1(c)), the concentration of the C24H32O7S2Na2 reaches a point to sufficiently chelate Ca2+ and Mg2+ ions but not to generate the deposits. In the steady potential state, the ions in the bulk solution continues to diffuse into the film pores in an incomplete sealing state, until the solute concentration reaches a balanced status between the inside and outside of the pores (with the concentration gradient reduced to 0).
Oxidation temperature: 20–25 °C;
Current density: 1.2 A dm−2;
And oxidation time: 30 min.
The thickness of the oxidation layer was controlled to be 12–15 μm. The nickel-free sealing processing was subsequently explored on the AAO film. The main steps for realizing this anodic oxidation and hole sealing are schematically illustrated in Fig. S1 of the ESI.† The compositions of the alkaline liquid used for washing the starting aluminum alloy plate were NaOH (5 g L−1), NaSiO3 (10–20 g L−1), Na3PO4 (10 g L−1), Na2CO3 (10–20 g L−1), and OP-10 (1 g L−1), while acidic washing liquid was comprised of H2SO4 (10%) and HNO3 (4%). The electrolyte used for electrochemical oxidation was a H2SO4 solution (186 g L−1). The rinsing was based on deionized (DI) water. The hole sealing treatment was conducted in a liquid bath mainly consisting of 2.5–10 g L−1 alkaline earth metal salt mixture (Ca(CH3COO)2·H2O and C4H6O4Mg·4H2O), 10–19 g L−1 triethanolamine (C6H15NO3), 0.25–1.0 g L−1 sodium dodecyl diphenyl ether disulfonate (C24H32O7S2Na2), and 2 g L−1 ammonium acetate (CH3COONH4). The solution adopted for electrochemical measurements was 3.5% NaCl.
(1) Upon optimization of the hole sealing formulation based on the alkaline earth metal salt, the optimal experimental parameters are obtained: (i) the concentrations of the salt mixture, complexant, surfactant, and buffer are suggested to be 10, 16, 0.5, and 2 g L−1, respectively; (ii) pH, temperature and sealing time are suggested to be 7, 85 °C, and 24–30 min, respectively. Under given conditions, the order of the impact of various experimental conditions on the weight loss of the sealed samples is given as follows: temperature > pH > salt mixture > surfactant > complexant.
(2) The electrochemical measurement of the self-corrosion current density reveals a higher corrosion resistance of the alkaline earth metal salt-sealed sample as compared to the conventional nickel salt-sealed sample. Over all the EIS test regions, the electrical resistance of the porous layer of the alkaline earth metal salt-sealed sample is higher than that of the nickel salt-sealed sample.
(3) Through tracking the E–t curve during hole sealing, it has been noted that raising the temperature can more quickly stabilize the potential over the temperature range of 70–85 °C. The higher pH value over the pH range of 5–7 make the potential more easily stabilized, while the potential cannot be stabilized at pHs larger than 7; the addition of surfactant, complexant, or buffer can help to quickly stabilize the potential, whereas the potential cannot be stabilized if without the addition of surfactant or complexant.
(4) This study has also discussed the mechanism underlying the effective hole sealing, with schematic illustration presented in Scheme 1.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c7ra10633e |
This journal is © The Royal Society of Chemistry 2017 |