Abstract
A several of basic ionic liquids (ILs) were synthesized as green solvents and catalysts for the preparation of 1,8-naphthyridyl derivatives via the Friedlander reaction. [Bmmim][Im] exhibited remarkable catalytic activity to achieve the synthetic targets, and the reaction conditions were optimized. The model product 2,3-diphenyl-1,8-naphthyridine (1,8-Nap), with carboxyethylthiosuccinic acid (CETSA) to form an IL corrosion inhibitor ([1,8-Nap][CETSA]), and its corrosion inhibition performance for Q235 steel in 1 M HCl were researched by weight loss measurements, and the results showed that the inhibition efficiency was 96.95% when the concentration of [1,8-Nap][CETSA] was 1 mM at 35 °C. The electrochemical test verified that [1,8-Nap][CETSA] acted as a mixed-type inhibitor but mainly exhibited cathodic behavior. The inhibitor adsorbed on the metal surface was further proved by surface topography analysis.
1. Introduction
1,8-Naphthyridine and its derivatives exhibit excellent optical performance,1−3 various biological activities,4 and flexible coordination ability,5−7 which led them to be widely used in many fields. As a kind of fluorescent biological probe, they have the characteristic of recognizing specific DNA sequences;8−10 good catalytic activity and thermal stability can be observed when they are used as a ligand for metal ions.11−13 Meanwhile, a large number of 1,8-naphthyridyl compounds own significant anti-inflammatory and antibacterial activity; especially, as anticancer agents, they have shown promising potential.14−16 Because 1,8-naphthyridyl derivatives have a broad range of applicability in many fields, there has been increasing attention toward developing efficient methods for 1,8-naphthyridine synthesis.
The common synthesis methods of 1,8-naphthyridine are Skraup, Combes, Pfitzinger, Conrad–Limpach, and Friedlander reactions over the past few decades;17−19 among them, the Friedlander reaction is considered to be the simplest method with higher yields.20−22 However, the Friedlander reaction system uses hazardous and often expensive acid or base catalysts; the catalysts cannot be reused, making it difficult for the reaction to realize industrialization. Thus, a convenient, rapid, environmentally friendly, and high-yielding synthetic method was designed using ionic liquids (ILs) as reaction media as well as promoters to synthesize 1,8-naphthyridine without any added catalyst or solution because ILs have interesting properties such as a wide liquidus range,23 good solubility of solutes,24 low saturated vapor pressure,25 and excellent catalytic activity and recyclability.26
1,8-naphthyridyl complexes with unique structures have been extensively applied in pharmaceuticals,27,28 molecular recognition,29 fluorescence sensors,30,31 as well as in the fields of organic chemistry.32 However, as far as we know, there are almost no reports about their use as a corrosion inhibitor. Therefore, we proposed 1,8-naphthyridine as a cation to synthesize an efficient corrosion inhibitor, and a new application of 1,8-naphthyridine was explored. In this study, ILs were used as reaction media to synthesize 1,8-naphthyridine by the Friedlander reaction and the influence of the IL type, reaction time, and reaction temperature on the reaction was investigated. The substrate compatibility of the reaction system under the optimal conditions was also researched. Then, 2,3-diphenyl-1,8-naphthyridine as the model substrate was used as the cation with the anion carboxyethylthiosuccinic acid (CETSA) to synthesize IL [1,8-Nap][CETSA] (Scheme 1),33 and its corrosion inhibition performance were researched by weight loss measurements, electrochemical tests, and surface topography analysis.
Scheme 1. Synthesis of [1,8-Nap][CETSA].
2. Results and Discussion
2.1. pH Measurement of ILs
The acid–base characterization of ILs is of great significance for application in the field of catalysis. By testing the acidity and alkalinity, the relationship between the anion and cation structure with alkalinity can be studied to guide the synthesis of ILs.34 Hence, the pH values of ILs with the concentration of 0.1 and 0.01 mol· L–1 were measured at 25 °C, and the results showed that alkalinity of the ILs [Bmmim][Im] > [Bmmim][OC2H5] > [Bmmim][OH] > [Bmmim][OCH3] at the same concentration.
2.2. Thermogravimetric Analysis of ILs
The thermal decomposition temperature of the ILs was measured by thermogravimetric analysis (TGA), and the results are shown in Figure 1. In addition, the values of Td5 and Td10 (Td5 and Td10 are the thermogravimetric temperatures of 5 and 10%)35−37 and char yield of ILs are listed in Table 1. The results display the percentage mass loss with temperature when the ILs are heated to a maximum temperature of 500 °C. Obviously, the initial weight loss peak appears at about 100 °C in Figure 1, and the Td5 and Td10 are between 56–94 and 84–207 °C, respectively, in Table 1, which may be caused by volatilization of water in the ILs and thus does not represent true decomposition. According to the thermogravimetric curve, there is a strong weight loss peak in the range of 150–300 °C, which may be caused by the decomposition of cations and anions of the ILs. Compared with other ILs, [Bmmim][OH] has a lower thermal decomposition temperature, and it is speculated that a smaller volume of OH– decomposes first. The results indicate that the four ILs have great thermal stability in the catalytic stage.
Figure 1.
TGA data of four basic ILs.
Table 1. TGA Data of the ILs.
samples | Td5 (°C) | Td10 (°C) | char yield (%) |
---|---|---|---|
[Bmmim][Im] | 64 | 112 | 3.57 |
[Bmmim][OH] | 56 | 85 | 5.80 |
[Bmmim][OC2H5] | 60 | 84 | 4.76 |
[Bmmim][OCH3] | 94 | 207 | 5.59 |
2.3. Synthesis of 1,8-Naphthyridine and Its Derivatives
Availing the ILs as the catalysts and solvents, the Friedlander reaction used 2-amino-3-pyridinecarboxaldehyde (a) and 2-phenylacetophenone (b) as the model substrates to investigate the catalytic competency of the ILs (Table 2). When the initial experiments were carried out with equimolar amounts of a and b in different ILs (5 mL) at 80 °C for 24 h, [Bmmim][Im] was found to be superior to others (entries 1–4); perhaps, [Bmmim][Im] has a stronger basicity. Moreover, we noted that only 5 mL of [Bmmim][Im] (entry 1) could obtain the product with great yield (entries 1 and 14–16). Then, encouraged by the stirring results, we further investigated the influence of other reaction conditions, such as reaction temperature (entries 1 and 5–7), reaction time (entries 1 and 8–10) and molar ratio (1 and 11–13). Surprisingly, the desired product was formed with 90% yield with a and b (0.6:1) in the presence of [Bmmim][Im] (5 mL) at 80 °C for 24 h (entry 12).
Table 2. Optimization of the Reaction Conditions Using the Model Friedlander Reaction between 2-Amino-3-pyridinecarboxaldehyde (a) and 2-Phenylacetophenone (b)a.
entry | catalyst | time (h) | T (°C) | IL (mL) | molar ratio (a/b) | yield (%) |
---|---|---|---|---|---|---|
1 | [Bmmim][Im] | 24 | 80 | 5 | 1:1 | 80 |
2 | [Bmmim][OH] | 24 | 80 | 5 | 1:1 | 54 |
3 | [Bmmim][OC2H5] | 24 | 80 | 5 | 1:1 | 55 |
4 | [Bmmim][OCH3] | 24 | 80 | 5 | 1:1 | 45 |
5 | [Bmmim][Im] | 24 | 40 | 5 | 1:1 | 56 |
6 | [Bmmim][Im] | 24 | 60 | 5 | 1:1 | 67 |
7 | [Bmmim][Im] | 24 | 100 | 53 | 1:1 | 74 |
8 | [Bmmim][Im] | 18 | 80 | 5 | 1:1 | 67 |
9 | [Bmmim][Im] | 21 | 80 | 5 | 1:1 | 71 |
10 | [Bmmim][Im] | 27 | 80 | 5 | 1:1 | 49 |
11 | [Bmmim][Im] | 24 | 80 | 5 | 0.4:1 | 73 |
12 | [Bmmim][Im] | 24 | 80 | 5 | 0.6:1 | 90 |
13 | [Bmmim][Im] | 24 | 80 | 5 | 0.8:1 | 88 |
14 | [Bmmim][Im] | 24 | 80 | 4 | 0.6:1 | 77 |
15 | [Bmmim][Im] | 24 | 80 | 6 | 0.6:1 | 59 |
16 | [Bmmim][Im] | 24 | 80 | 3 | 0.6:1 | 62 |
Reaction conditions: a and b (1 mmol) were dissolved in ILs.
At the end of the reaction, [Bmmim][Im] was easily recovered from the mixture by a simple extraction with deionized water, and its reusability was researched under the same reaction conditions. It was noticed that the recovered catalyst was reused 4 times without significant loss of its catalytic activity (Figure 2).
Figure 2.
Recyclability of [Bmmim][Im] for the synthesis of 2,3-diphenyl-1,8-naphthyridine.
Thereafter, according to the suitable reaction conditions of this method, the substrate compatibility of the Friedlander reaction system was investigated, so 2-amino-3-pyridinecarboxaldehyde was reacted with various acyclic and cyclic ketones (aldehydes) to produce a range of 1,8-naphthyridyl derivatives, and the results are displayed in Table 3. As shown, the reaction was successful with cyclic ketones such as cyclohexanone and 2-methylcyclohexanone (entries 1 and 2), and it achieved the desired products with moderate yield. Likewise, polycyclic 1,8-naphthyridine 3g–h were obtained under basic IL conditions with a simple workup. Frequently, the Friedlander reaction with unsymmetrical ketones may undergo two modes of cyclization, producing different natures of catalysts. Surprisingly, the [Bmmim][Im]-catalyzed Friedlander reaction with unsymmetrical ketones (aldehydes) generated exclusive products in excellent yields (entries 3 and 5). All desired products of substituted 1,8-naphthyridine were obtained and characterized by 1H NMR and 13C NMR spectra.
Table 3. Preparation of 1,8-Naphthyridyl Derivativesa.
Reaction conditions: 1a (0.6 mmol) and 2 (1 mmol) were dissolved in 5 mL of [Bmmim][Im] at 50 °C for 24 h.
2.4. Mechanism
According to all the experiments, we put forward a possible reaction mechanism of the Friedlander reaction shown in Scheme 2. First, the ketone (aldehyde) with α-H (a) generates carbanion (c) under alkaline conditions, and (c) undergoes a condensation reaction with carbonyl-containing aldehyde (d) to form an intermediate product (f), and finally, the produce ring is formed while the carbon–nitrogen double bond generates (h).22,38
Scheme 2. Proposed Mechanism for the Synthesis of 1,8-Naphthyridyl Derivatives.
3. Application of 1,8-Naphthyridines
3.1. Weight Loss Measurements
In order to know the corrosion protection behavior with different concentrations of [1,8-Nap][CETSA], we performed the weight loss measurements for Q235 steel in 1 M HCl for 24 h at 35 °C, and the results are shown in Table 4. All measurements were repeated 3 times under the same condition. The corrosion rate (V), inhibition efficiency (η), and surface coverage (θ) were calculated from the following equations.33
![]() |
1 |
![]() |
2 |
![]() |
3 |
where Δm represents the weight loss value of the Q235 steel sample after the weight loss measurement (g), t is the immersion time (h), s is the immersed area of the steel sample (m2), V0 and Vinh are the corrosion rates without and with [1,8-Nap][CETSA], respectively (g·m–2·h–1).
Table 4. Corrosion Parameters of Q235 Steel Immersed in 1 M HCl Solution in the Absence and Presence of Different Concentrations of [1,8-Nap][CETSA] for 24 h at 35 °C.
C (mM) | V (g·m–2 h–1) | η (%) | θ |
---|---|---|---|
blank | 12.55 ± 0.04 | ||
0.1 | 0.50 ± 0.02 | 95.99 | 0.9599 |
1 | 0.38 ± 0.02 | 96.95 | 0.9695 |
2.5 | 0.42 ± 0.05 | 96.58 | 0.9658 |
5 | 0.47 ± 0.03 | 96.18 | 0.9618 |
It can be seen from Table 4 that the inhibition efficiency increased with the increase of [1,8-Nap][CETSA] and reached up to 96.95% when the concentration was 1 mM; probably, inhibitor molecules adsorbed on the Q235 steel’s surface and excluded the corrosion media. Meanwhile, the inhibitor could affect either or both metal dissolution and hydrogen evolution processes.39 However, with the concentration of [1,8-Nap][CETSA] continuously increasing, the inhibition efficiency decreased slightly. Perhaps, this was due to the competitive adsorption of inhibitor molecules on the metal surface. Compared to the previous literature, [1,8-Nap][CETSA] and other corrosion inhibitors, such as choline-based and imidazolium-based ILs, showed excellent corrosion inhibition ability at high concentration, but [1,8-Nap][CETSA] exhibited better inhibition efficiency when it was at low concentration.39−42 This proves that [1,8-Nap][CETSA] ILs have significant application potential in the corrosion protection field.
3.2. Potentiodynamic Polarization Measurements
Potentiodynamic polarization curves for Q235 steel in 1 M HCl in the absence and presence of different concentrations of [1,8-Nap][CETSA] at 35 °C are shown in Figure 3. The inhibition efficiency (η) and the degree of surface coverage (θ) were determined from eq 4, and calculated parameters are gathered in Table 5, where Ecorr is the corrosion potential, and Icorr0 and Icorr are the corrosion current densities in the absence and presence of the inhibitor, respectively.43,44
![]() |
4 |
Figure 3.
Polarization curves of Q235 steel in 1 M HCl in the absence and presence of different concentrations of [1,8-Nap][CETSA].
Table 5. Polarization Parameters for Q235 Steel in 1 M HCl Solution in the Absence and Presence of Different Concentrations of [1,8-Nap][CETSA].
medium | Ecorr (mV) | Icorr (μA·cm–2) | η (%) | θ |
---|---|---|---|---|
blank | –457 ± 3 | 64.7 ± 0.02 | ||
0.1 | –464 ± 4 | 10.13 ± 0.03 | 84.34 | 0.8434 |
1 | –458 ± 1 | 7.00 ± 0.02 | 89.18 | 0.8918 |
2.5 | –465 ± 3 | 9.05 ± 0.03 | 86.01 | 0.8601 |
5 | –459 ± 2 | 11.22 ± 0.01 | 82.65 | 0.8265 |
As can be seen in Figure 3, all the anodic and cathodic Tafel curves moved to the lower current direction and the curves were almost parallel to the blank curve upon the addition of the inhibitor; this indicated that the inhibitor reduced the anodic dissolution of steel and delayed the cathodic reaction of hydrogen evolution, but the inhibition mechanism had not been altered. If the change in the Ecorr value in the presence of the inhibitor is more than ±85 mV related to the Ecorr value of blank, the inhibitor may be considered as a cathodic or anodic type. The inhibitor can be deemed as a mixed type when the shift is not more than 85 mV in Ecorr.45−47 The data in Table 5 show that Ecorr shifts slightly toward the negative direction and the displacement was less than 85 mV with the inhibitor existence, which means that [1,8-Nap][CETSA] is a mixed-type inhibitor but mainly exhibits cathodic behavior.
3.3. Electrochemical Impedance Spectroscopy
Electrochemical impedance spectroscopy (EIS) is a method for finding out the mechanism involved in the corrosion process. The different processes occurring at the electrode/electrolyte interface can be simulated with equivalent electrical circuits, and these models are used to adjust the experimental impedance maps and extract parameter values.48 The Nyquist and Bode plots of Q235 steel immersed in 1 M HCl solution without and with various concentrations of [1,8-Nap][CETSA] at 35 °C are represented in Figures 4 and 5, and the equivalent electrical circuits are shown in Figure 6.
Figure 4.
Nyquist plot of Q235 steel in 1 M HCl solution without and with different concentrations of [1,8-Nap][CETSA].
Figure 5.
Bode plots for Q235 steel without and with different concentrations of [1,8-Nap][CETSA] in 1 M HCl solution.
Figure 6.
Equivalent circuit used to fit impedance spectra.
As seen in the Nyquist spectra, the diameter of the semicircle increases in the presence of [1,8-Nap][CETSA], which shows that the inhibitor molecules adsorbed onto the surface of Q235 steel and hindered the charge-transfer process to decrease the corrosion rate. However, the shape of the capacitor ring did not alter, indicating that the corrosion inhibition mechanism did not change. From the Bode plots (Figure 5), it was apparently seen that the values of the phase angle increased with the addition of [1,8-Nap][CETSA] due to the formation of a significant covering layer on the electrode’s surface.
Table 6 lists a series of EIS measurement parameters such as the solution resistance (Rs), charge-transfer resistance (Rct), electric double-layer capacitance (Cdl), and inhibition efficiency (η). Because of inhibitor’s adsorption mode and the difference in surface roughness, a constant-phase element was employed rather than an ideal double-layer capacitor in order to gain a more accurate model.42 The values of inhibition efficiency and double-layer capacitance were computed from eqs 5 and 6, respectively.49
![]() |
5 |
![]() |
6 |
where Rct and Rct0 are the resistances of charge transfer with and without [1,8-Nap][CETSA], respectively.
Table 6. Impedance Parameters for Q235 Steel in 1 M HCl in the Presence and Absence of Different Concentrations of [1,8-Nap][CETSA].
medium | Rs (Ω cm2) | Rct (Ω cm2) | Cdl (μF·cm–2) | n | η (%) |
---|---|---|---|---|---|
blank | 0.83 ± 0.033 | 13.21 ± 0.9 | 406.81 | 0.80 ± 0.04 | |
0.1 | 0.71 ± 0.020 | 146.5 ± 1.6 | 175.73 | 0.70 ± 0.03 | 91.16 |
1 | 0.73 ± 0.0091 | 188.7 ± 2.0 | 162.33 | 0.70 ± 0.03 | 92.99 |
2.5 | 0.70 ± 0.03 | 185.2 ± 1.1 | 159.02 | 0.71 ± 0.01 | 92.86 |
5 | 0.67 ± 0.015 | 168.6 ± 2.8 | 136.14 | 0.70 ± 0.02 | 92.16 |
It is observed that Rct values increase significantly in the presence of [1,8-Nap][CETSA], while the Cdl value decrease is probably attributed to the replacement of water and HCl molecules with large dielectric constants of [1,8-Nap][CETSA] molecules;50 these results illustrate that a protective layer formed on the metal surface to inhibit the corrosion process. Meanwhile, the EIS measurement showed that η was over 90%, and inhibitor molecules can be stably adsorbed on the surface of Q235 steel.
3.4. Surface Topography Analysis
Scanning electron microscopy (SEM) and energy-dispersive spectroscopy (EDS) are useful techniques used to detect and analyze the morphology and elemental composition of the Q235 steel surface in different situations.51,52 The SEM and EDS graphs of Q235 steel immersed in 1 M HCl solution without or with 1 mM [1,8-Nap][CETSA] for 24 h at 35 °C are presented in Figure 7. In Figure 7a, the freshly polished mechanical marks on the surface of the carbon steel can be observed. In the absence of inhibitors (Figure 7b), the Q235 steel surface became rough and uneven due to the corrosive attack by HCl solution. Figure 7c shows that Q235 steel was protected with [1,8-Nap][CETSA], and the steel surface appeared smooth and uniform without distinct corrosion pits, and even signs of sandpaper polishing could be clearly seen. The phenomenon suggested that the inhibitor molecules on the surface of Q235 steel resulted in the formation of a protective film, confirming the previous experimental results.
Figure 7.
SEM images and EDS spectra of Q235 steel samples before (a) and after immersion in 1 M HCl without (b) and with (c) 1 mM [1,8-Nap][CETSA] for 24 h at 35 °C.
The EDS spectrum was used to further analyze the surface elemental composition of Q235 steel. On comparing Figure 7b with Figure 7a, the existence of Cl atoms covering the metal surface can be observed, which can be attributed to the formation of corrosion products. The EDS spectra in the corrosion-inhibiting medium (Figure 7c) pointed out the presence of O linked to the [1,8-Nap][CETSA] adsorbed on the metal surface, forming a protective layer.
4. Conclusions
In summary, we have successfully conceived a green method for the synthesis of 1,8-naphthyridyl derivatives by the Friedlander reaction, which used a series of basic ILs such as [Bmmim][Im] as an efficient catalyst under solvent-free conditions. The optimized reaction conditions of this method were as follows: α-methylene carbonyl compounds and 2-amino-3-pyridinecarboxaldehyde at a molar ratio of 1:0.6; they were dissolved in 5 mL of [Bmmim][Im] at 80 °C for 24 h, and the IL was reused at 4 times without significant loss of its catalytic activity. Therefore, we proposed a possible mechanism based on the experimental results. This method not only provides a simple, excellent, and moderate way to generate 1,8-naphthyridyl derivatives but also to reduce environmental pollution. In addition, the model substrate 2,3-diphenyl-1,8-naphthyridine with CETSA forms a corrosion inhibitor [1,8-Nap][CETSA]. The inhibition performance of [1,8-Nap][CETSA] on Q235 steel in 1 M HCl were studied via weight loss tests, electrochemical measurements, and surface topography analysis. The consequence suggested that inhibitor molecules adsorbed on the surface of the metal and formed a dense protective layer, which blocked the contact between metal and acid solution. At the same time, the results confirmed that [1,8-Nap][CETSA] showed mixed corrosion inhibition but mainly exhibited cathodic behavior.
5. Experimental Section
5.1. Materials
1,2-Dimethyl imidazole, bromobutane, imidazole, sodium methoxide, sodium ethanol, α-methylene ketones (aldehydes), sodium hydroxide, and 2-amino-3-pyridine formaldehyde were purchased from Shanghai Yi Heng Technology Co., Ltd. Ethyl acetate and petroleum ether were purchased from Beijing Chemical Plant. Hydrochloric acid was purchased from Tianjin Chemical Works. CETSA was synthesized in our lab.
5.2. Synthesis of Basic ILs
The basic ILs [Bmmim][Im], [Bmmim][OH], [Bmmim][OC2H5], and [Bmmim][OCH3] were prepared according to the reported procedures.53,54
5.3. Synthesis of 1,8-Naphthyridine
A mixture of α-methylene carbonyl compounds and 2-amino-3-pyridinecarboxaldehyde in ILs was added into a Schlenk reaction bottle and magnetically stirred at about 80 °C. After the reaction, the rection mixture was extracted by moderate ethyl ether and deionized water. The ethyl ether phase was collected, and then it was evaporated under a rotary evaporator to obtain the crude product. 1,8-Naphthyridine was separated using a specific volume ratio of the solvent (petroleum ether/ethyl ether) by silica gel column chromatography.
5.4. Synthesis of [1,8-Nap][CETSA]
A total of 4.44 g of CETSA and 2.8 g of 2,3-diphenyl-1,8-naphthyridine were dissolved in 15 mL of methanol. The reaction mixture was stirred and heated to 50 °C for 5 h. After the reaction, the mixture was distilled under vacuum to remove methanol and to obtain [1,8-Nap][CETSA] with a yield of 91%.
5.5. Weight Loss Measurements
The dimensions of the Q235 steel sample used for weight loss measurement were 25 mm × 25 mm × 1 mm, and the steel pieces were polished, cleaned by deionized water, anhydrous ethanol, and acetone, dried in warm air, and then weighed for the test. The Q235 steel sample was immersed in 1 M HCl solution without or with different concentrations of the inhibitors at 35 °C. After 24 h, the immersed Q235 steel samples were washed and reweighed.
5.6. Electrochemical Measurements
Potentiodynamic polarization curves and EIS are two classical electrochemical techniques which were used to analyze the inhibition characteristics of [1,8-Nap][CETSA] in 1 M HCl at 35 °C. Electrochemical experiments were carried out through a conventional three-electrode system, with the Q235 steel sample as a working electrode and saturated Hg/HgCl2 and platinum sheet as reference and counter electrodes, respectively. The working electrode was immersed in 1 M HCl solution for 30 min to ensure a stationary condition. Polarization curves were verified at a potential range of ±250 mV with a scan rate of 0.5 mV·s–1. Impedance experiments were carried out in the frequency range from 100 kHz to 100 mHz by using an amplitude of 15 mV. All experiments were replicated 3 times.
5.7. Characterization
The thermal stability of the IL was determined by TGA. Under the protection of nitrogen, the heating rate was 10 °C/min, and the test temperature range was 0–500 °C. The alkalinity of the IL was determined by a pH meter, and the pH value of the IL of different concentrations was measured at 25 °C. The structures of ILs, 1,8-naphthyridyl derivatives, and [1,8-Nap][CETSA] were confirmed by 1H NMR, 13C NMR, Fourier transform infrared spectroscopy, and high-resolution mass spectroscopy. The corrosion inhibition performance of [1,8-Nap][CETSA] was determined by the electrochemical measurements without and with different concentrations of corrosion inhibitors at 35 °C. SEM and EDS were used to study the surface morphology of the Q235 steel specimens (10 mm × 10 mm × 1 mm) that were immersed in 1 M HCl solution in the absence and presence of 1 mM [1,8-Nap][CETSA] for 24 h at 35 °C. Potentiodynamic polarization curves and EIS were used to determine the corrosion inhibition characteristics of [1,8-Nap][CETSA] in 1 M HCl solution.
Acknowledgments
We are grateful to the support from the Jilin Province Science and Technology Development Plan Project (20180201019SF) and the Doctor Startup Foundation of the Jilin Institute of Chemical Technology.
Supporting Information Available
The Supporting Information is available free of charge at https://pubs.acs.org/doi/10.1021/acsomega.1c04103.
pH measurement of ILs and chemical structure characterization of Friedlander reaction products and ILs (PDF)
The authors declare no competing financial interest.
Supplementary Material
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