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Callister - An introduction - 8th edition

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17.4 Prediction of Corrosion Rates • 687<br />

Overvoltage, c<br />

+<br />

0<br />

–<br />

i L<br />

Figure 17.9 For reduction reactions,<br />

schematic plots of overvoltage versus<br />

logarithm of current density for<br />

(a) concentration polarization, and<br />

(b) combined activation–concentration<br />

polarization.<br />

Log current density, i<br />

(a)<br />

+<br />

0<br />

i 0<br />

Overvoltage, <br />

–<br />

Activation<br />

polarization<br />

Concentration<br />

polarization<br />

Log current density, i<br />

(b)<br />

i L<br />

of current density until i approaches i L ; at this point, c decreases abruptly in<br />

magnitude.<br />

Both concentration and activation polarization are possible for reduction reactions.<br />

Under these circumstances, the total overvoltage is just the sum of both<br />

overvoltage contributions. Figure 17.9b shows such a schematic -versus-log i plot.<br />

Concept Check 17.3<br />

Briefly explain why concentration polarization is not normally rate controlling for<br />

oxidation reactions.<br />

[The answer may be found at www.wiley.com/college/callister (Student Companion Site).]<br />

Corrosion Rates from Polarization Data<br />

Let us now apply the concepts just developed to the determination of corrosion rates.<br />

Two types of systems will be discussed. In the first case, both oxidation and reduction<br />

reactions are rate limited by activation polarization. In the second case, both<br />

concentration and activation polarization control the reduction reaction, whereas<br />

only activation polarization is important for oxidation. Case one will be illustrated<br />

by considering the corrosion of zinc immersed in an acid solution (see Figure 17.1).

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