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Final Report - Strategic Environmental Research and Development ...

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Corrosion rate ( 1/R<br />

p<br />

) ohm -1 cm -2<br />

Corrosion rate ( 1/R<br />

p<br />

) ohm -1 cm -2<br />

10 -4<br />

10 -3 2 3 4 5 6 7<br />

decarbonated <strong>and</strong> uninhibited case<br />

10 -4<br />

10 -5<br />

7 h<br />

22 h<br />

44 h<br />

65 h<br />

83 h<br />

94 h<br />

10 -5<br />

10 -3 2 3 4 5 6 7 8<br />

decarbonated <strong>and</strong> inhibited case<br />

6 h<br />

27 h<br />

43 h<br />

64 h<br />

86 h<br />

108 h<br />

10 -6<br />

10 -6<br />

pH<br />

(a)<br />

(b)<br />

Figure 3.29. The corrosion rate of 2024-T3 coupons immersed in decarbonated (a)<br />

sodium chloride solutions (b) zinc containing sodium chloride solutions at different pH<br />

(obtained from the EIS measurements).<br />

XPS surface analysis results are consistent with this idea where negligible carbonate hydroxide<br />

compound was seen on the sample in decarbonated pH 4 Zn 2+ -containing solutions, in contrast to<br />

the aerated pH 4 Zn 2+ -containing solution which had a relatively higher concentration of the<br />

carbonate compound. Hence, CO 2 -bearing precipitation aids in retarding the corrosion reactions<br />

in Zn 2+ -containing chloride solutions.<br />

5.3.2.5.3 Mechanism of inhibition. A mechanism is proposed to explain the inhibition by the<br />

Zn 2+ in acidic (pH 3), mildly acidic (pH 4) <strong>and</strong> neutral (pH 7) environments. AA 2024-T3 is<br />

passivated at pH 7 except at the intermetallic particles as the oxide film is much thinner at the<br />

intermetallic particles. The alloy is susceptible to localized corrosion due to galvanic coupling<br />

between the Cu-rich sites within the intermetallic particle <strong>and</strong> the anodic constituents of the<br />

active intermetallics or between the Cu-rich sites <strong>and</strong> the matrix surrounding the intermetallic<br />

particles. These Cu-containing particles support ORR <strong>and</strong> dissolve the matrix surrounding the<br />

particle leading to pitting or trenching of the alloy or dealloying of the active intermetallics [8].<br />

ORR leads to an increase in alkalinity <strong>and</strong> drives the local pH on the intermetallic particle<br />

upwards. This local increase in pH lowers the solubility of Zn 2+ cation adjacent to the<br />

intermetallic particles resulting in massive precipitation, which eventually leads to exhaustion of<br />

the Zn 2+ ion. Corrosion process is followed by precipitation. Higher corrosion rate is seen at<br />

shorter periods of exposure time <strong>and</strong> then a decrease in the corrosion rate results due to increased<br />

precipitation with increase in exposure time as seen in Figure 3.27b. This decrease in the<br />

corrosion rate was observed after the formation of an effective physical barrier to ORR, which<br />

causes localized inhibition. The massive localized precipitation was evidenced in the SEM<br />

pictures of the free corrosion sample in pH 7 solution where the entire surface was covered with<br />

crystalline deposits of Zn-Al carbonate hydroxide. The deposits were densely populated over the<br />

intermetallics <strong>and</strong> had openings or defects at pits, trenches in <strong>and</strong> around the intermetallic<br />

particles, through which corrosion can continue to occur.<br />

Al dissolves in acidic pH seen in the Pourbaix diagrams. The entire surface of the Al alloy is<br />

activated at pH 4 including the intermetallic particles <strong>and</strong> the matrix. The alloy is subjected to<br />

pH<br />

139

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