The corrosion behavior of Zn and Zn-Al plating samples was investigated based on the measurement of anodic and cathodic polarization curves, the change in potential with use of a constant current of 2mA, the observation of structures in a cross section after a corrosion test, and the identification of corrosion products in the samples. Two plating samples were examined. One was fabricated by the dipping of the steel in a Zn bath at 743K for 60s, and another was fabricated by dipping steel in a secondary Zn-Al bath at 693K for 60s after first dipping in a Zn bath. The potentiostatic corrosion was carried out in a 3% by NaCl aqueous solution at 303K with a potential scan rate of 30mv/min and Ag/AgCl was used for the reference electrode. The galvanostatic corrosion was carried out in a 0.5% by NaCl aqueous solution with a constant current of 2mA/dm2. The change in the potential of the sample was measured, After the corrosion test, the samples were examine using EPMA and X-RD, Polarization curves obtained indicated that the reaction of Zn and Zn-Al coatings was controlled by control of the cathodic reaction. The rate of the cathodic reaction was faster for the Zn-Al coating than for the Zn coating. The same tendency was observed with Zn-Al alloy layer (Fe4Al13-Zn) and Zn alloy layer (ζ). During galvanostatic corrosion, corrosion proceeding through the η phase was observed between the lamellar ζ phase in the Zn plating sample. The contrast, the Fe4Al13-Zn phase dispersed in a Zn-Al matrix in the Zn-Al plating sampls, and the corrosion path was more complicated than with in the Zn plating sample. The time to reach galvanosttic corrosion of the base metal is thus believed to be determined by the difference in the corrosion path.
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