In order to evaluate the corrosion protection ability of the synthesized LDH-NO
2- on the carbon steel, it was added into 0.02 mol/L NaCl with a concentration of 5g/L. For comparison, the EIS measurements of carbon steel in blank NaCl solution and in NaCl solution with 5 g/L LDH were also performed. The EIS results were recorded in an immersion duration of 7 d. Both the Nyquist and Bode plots were presented in
Figure 6. According to
Figure 6a1–b1 and
Figure 6a2–b2, the impedance arc of the sample in blank NaCl solution and in NaCl solution with 5 g/L LDH decreased remarkably after immersion of 1 days in comparison with that of 2 h. The impedance presented a decreasing trend in this immersion period of 7 d in spite of some small fluctuations. According to
Figure 6b1–b2, the impedance values at 0.01 Hz of the carbon steel in NaCl solution with 5 g/L LDH were more than one magnitude larger than that of the carbon steel in blank NaCl solution, which may be due to the chloride adsorption effect based on the anion exchange characteristic and the enhanced physical barrier effect caused by the plate-like morphology of LDH. In addition, the phase angle peak in
Figure 6c2 was much broader than that in
Figure 6c3, indicating certain corrosion protection of LDH powder in NaCl solution towards the carbon steel. When LDH-NO
2- was added in the 0.02 M NaCl solution (
Figure 6a3–b3), the obtained impedance arc became much larger than that in the blank NaCl solution and the NaCl solution with addition of 5g/L LDH. The impedance values at the low frequency of 0.01 Hz was one magnitude larger than that of the carbon steel immersed in NaCl solution with addition of 5g/L LDH, indicating enhanced corrosion protection effect of LDH-NO
2- compared with that of LDH. Accordingly, the phase angle peak in
Figure 6c3 was much broader than that in
Figure 6c2. The equivalent circuit containing one time constant in
Figure 6d was used to fit the EIS data, where
Rs was solution resistance, the
Rct was the charger transfer resistance related to the electrochemical corrosion reaction and the
Qdl meant the double layer capacitance, which was used here to replace an ideal capacitor due to the non-homogeneity of the carbon steel surface in this system [
33]. The Fitting results of the above EIS data were shown in
Figure 6e,f. According to
Figure 6e, the
Rct values of the sample immersed in NaCl solution with 5 g/L LDH-NO
2- indicated a slightly rising trend with the increased immersed time and at least one magnitude higher than other samples, in contrast, the
Rct values of the sample immersed in blank NaCl solution and in NaCl solution decreased continuously. In addition, the
Cdl values of various samples presented a different trend in comparison with that of
Rct values. According to the literature,
Cdl measures the numbers of the electrochemically active sites in the coating/substrate interface [
26,
34]. The
Cdl of the carbon steel in blank NaCl solution presented the largest values and the corresponding value of the carbon steel in NaCl solution with 5 g/L LDH was lower, however, this value was still larger than that of carbon steel in NaCl solution with 5 g/L LDH-NO
2-. This result indicated that corrosion can be effectively prevented in the presence of LDH-NO
2- in this system. In Figure S1, after the addition of LDH-MoO
42-, the corrosion resistance of the carbon steel was a little bit larger than that of the carbon steel in blank solution and much smaller than that of the sample with LDH and LDH-NO
2-, which can be probably due to the formation of CaMoO
4 as verified in the SEM results in
Figure 3 and the XRD results in
Figure 4. Therefore, this product was not added in the epoxy coating for further corrosion test. However, the above result could provide instruction significance in the future LDH modification and some specific inhibitor was nor suitable for modification of certain LDH due to the possible reactions.