21-Mat-A7 Environmental Degradation of Materials · May 2015
Question 1 of 6: Basic Corrosion Theory
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. National Exams, May 2015 — 10-Met-A7, Corrosion and Oxidation. Three hours, closed book, approved Casio/Sharp calculator only. Six questions of 20 marks each; the rubric states that five of the six constitute a complete paper (100 marks). All six are answered below. The rubric also notes that several questions require descriptions of types of corrosion and engineering solutions, and that clarity and organisation of the answer are marked — the essay answers below are written as structured prose for that reason.
Reference texts. The answers below are keyed to the works normally recommended for this syllabus code:
M. G. Fontana, Corrosion Engineering, 3rd ed. — electrochemical corrosion theory, polarization and passivity (Ch. 6), forms of corrosion: galvanic, crevice, pitting, intergranular, stress corrosion cracking (Ch. 3), cathodic and anodic protection (Ch. 4–9).
D. A. Jones, Principles and Prevention of Corrosion, 2nd ed. — thermodynamics and the Nernst equation (Ch. 2–3), kinetics and polarization diagrams (Ch. 4), environmental cracking and corrosion fatigue (Ch. 10–11), coatings and cathodic protection (Ch. 13–14).
W. D. Callister and D. G. Rethwisch, Materials Science and Engineering: An Introduction, 10th ed. — corrosion and degradation of materials (Ch. 17).
ASM Handbook, Vol. 13A (Corrosion: Fundamentals, Testing, and Protection) — forms of corrosion, coatings and cathodic protection practice.
NACE SP0169 (buried pipeline cathodic protection) and NACE/AMPP standards on impressed-current and sacrificial-anode design, cited where relevant to Question 6(b).
Given. Two reduction half-reactions with their standard (1 M, 1 atm, 25 °C) potentials, and the actual service condition of a neutral aerated solution.
Given data — Question 1(a)
Quantity
Symbol
Value
Oxygen reduction half-cell
$O_2+4e^-+4H^+\rightarrow 2H_2O$
$E^\circ=1.229$ V, $n=4$
Ferrous-hydroxide reduction half-cell
$Fe(OH)_2+2e^-+2H^+\rightarrow Fe+2H_2O$
$E^\circ=-0.048$ V, $n=2$
Solution pH
$pH$
7 (so $[H^+]=10^{-7}$ M)
Oxygen partial pressure
$p_{O_2}$
0.2 atm
Nernst constant at 25 °C
$2.303RT/F$
0.0592 V (as quoted on the paper)
Find. The actual (non-standard) electrode potential of each half-cell at pH 7 and $p_{O_2}=0.2$ atm.
Approach. Apply the Nernst equation $E=E^\circ-\dfrac{0.0592}{n}\log Q$ to each half-cell as written (a reduction), with $Q$ built from the activities of the species that appear explicitly: $O_2$ as its partial pressure, $H^+$ as $10^{-pH}$, and the two solids ($Fe$, $Fe(OH)_2$) at unit activity.
Oxygen half-cell. For $O_2+4H^++4e^-\rightarrow 2H_2O$ the reaction quotient for the reduction is $Q=1/\big(p_{O_2}[H^+]^4\big)$ ($H_2O$ at unit activity), so
$$E_{O_2/H_2O} \;=\; E^\circ_{O_2/H_2O} - \frac{0.0592}{4}\log\!\left(\frac{1}{p_{O_2}[H^+]^4}\right) \;=\; E^\circ_{O_2/H_2O} + \frac{0.0592}{4}\log p_{O_2} - 0.0592\,pH$$
Substituting $p_{O_2}=0.2$ and $pH=7$,
$$E_{O_2/H_2O} \;=\; 1.229 + \frac{0.0592}{4}\log(0.2) - 0.0592(7) \;=\; 1.229 - 0.0103 - 0.4144$$
$$\boxed{E_{O_2/H_2O} \;\approx\; 0.804\ \text{V}}$$
Dropping the pH from 0 (standard, acidic) to 7 costs the oxygen electrode $0.0592\times7=0.414$ V — by far the larger of the two corrections — while the depressed oxygen activity ($p_{O_2}=0.2$ instead of 1 atm) costs only about 10 mV.
Ferrous-hydroxide half-cell. For $Fe(OH)_2+2H^++2e^-\rightarrow Fe+2H_2O$, $Fe$ and $Fe(OH)_2$ are both solids at unit activity, so $Q=1/[H^+]^2$ and
$$E_{Fe(OH)_2/Fe} \;=\; E^\circ_{Fe(OH)_2/Fe} - \frac{0.0592}{2}\log\!\left(\frac{1}{[H^+]^2}\right) \;=\; E^\circ_{Fe(OH)_2/Fe} - 0.0592\,pH$$
$$E_{Fe(OH)_2/Fe} \;=\; -0.048 - 0.0592(7) \;=\; -0.048-0.4144$$
$$\boxed{E_{Fe(OH)_2/Fe} \;\approx\; -0.462\ \text{V}}$$
This half-cell has no $O_2$ term at all, so its entire shift from standard conditions is the $-0.0592\,pH$ term — the same 414 mV correction as above, because both half-reactions consume the same number of protons per electron (1:1).
Final results — Question 1(a)
Half-cell
Symbol
Result
Oxygen reduction
$E_{O_2/H_2O}$
$+0.804$ V
Ferrous hydroxide reduction
$E_{Fe(OH)_2/Fe}$
$-0.462$ V
1.2 — (b) The overall corrosion reaction, $E_{corr}$, and spontaneity
Find. The overall (rusting) reaction obtained by combining the two half-cells, the resulting corrosion cell potential $E_{corr}$, and whether the reaction proceeds spontaneously as written.
Approach. In the corrosion cell, iron is oxidised (the anodic reaction, the reverse of the printed $Fe(OH)_2/Fe$ reduction) and oxygen is reduced (the cathodic reaction, exactly as printed). Balance electrons between the two half-reactions, add them, and evaluate $E_{corr}=E_{cathode}-E_{anode}$ using the two Nernst-corrected potentials from part (a) — the anode's potential is still taken from its own reduction half-reaction, not reversed in sign, because that is how the cell-potential formula is defined.
Balance the electrons and add the half-reactions. The oxygen reduction needs 4 electrons; the iron oxidation (reversed ferrous-hydroxide half-cell) supplies only 2, so the anodic half-reaction is doubled:
$$2Fe + 4H_2O \;\longrightarrow\; 2Fe(OH)_2 + 4H^+ + 4e^- \qquad \text{(anodic, oxidation, }\times 2\text{)}$$
$$O_2 + 4H^+ + 4e^- \;\longrightarrow\; 2H_2O \qquad \text{(cathodic, reduction)}$$
Adding and cancelling the $4H^+$ and $2H_2O$ common to both sides gives the overall corrosion reaction
$$\boxed{2Fe + O_2 + 2H_2O \;\longrightarrow\; 2Fe(OH)_2}$$
which is mass-balanced (2 Fe, 4 O, 4 H on each side) and is exactly the familiar first step of the rusting of iron: ferrous hydroxide, which then oxidises further in air to the hydrated ferric-oxide "rust" the question refers to.
Evaluate the corrosion cell potential. With oxygen reduction as the cathode and the ferrous-hydroxide couple as the anode,
$$E_{corr} \;=\; E_{cathode}-E_{anode} \;=\; E_{O_2/H_2O}-E_{Fe(OH)_2/Fe} \;=\; 0.804-(-0.462)$$
$$\boxed{E_{corr} \;\approx\; +1.267\ \text{V}}$$
Test spontaneity. The free-energy change for the reaction as balanced (4 electrons transferred) is
$$\Delta G \;=\; -nFE_{corr} \;=\; -(4)(96\,490\ \text{C/mol})(1.267\ \text{V}) \;\approx\; -489\ \text{kJ}$$
Because $E_{corr}>0$, $\Delta G<0$: the reaction is spontaneous as written. Physically this says the oxygen half-cell's potential remains well above the iron half-cell's potential even after both are corrected to the actual pH and oxygen activity of the service solution, so iron sitting in neutral aerated water has a large thermodynamic driving force to rust — consistent with everyday experience, and with the fact that neither half-cell needed to be reversed in sign to build a positive-$E_{corr}$ cell.