Question 5 of 8: Cu Concentration Cell and Carbon Diffusion in FCC Iron
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exam 04-BS-11, Properties of Materials — May 2014. 3 hours,
closed-book examination (approved Casio or Sharp calculator only). Any five questions constitute
a complete paper; only the first five questions as they appear in the answer book are marked. All
eight questions are solved below for completeness.
Given. (a) $E^\circ_{Cu}=+0.337$ V, $n=2$; $C_1=0.03\ M$, $C_2=0.002\ M$
Cu$^{2+}$. (b) Surface concentration 1 C atom / 40 unit cells; concentration at $x=2$ mm, 1 C atom /
50 unit cells; $D=3\times10^{-11}\ \text{m}^2/\text{s}$; FCC iron, $a_0=0.365$ nm.
Find. (a)(i) Which end corrodes. (a)(ii) Potential difference. (b) Carbon
atoms diffusing through each unit cell per minute.
Approach
Part (a) is a concentration cell: with identical electrode material at both ends, the Nernst
equation gives a potential difference driven purely by the ion-concentration difference, and
thermodynamics dictates that the electrode in the more dilute solution is the one that must
oxidize (corrode) to restore equilibrium. Part (b) applies Fick's first law directly, converting
the given "atoms per unit cell" concentrations into a true volumetric concentration using the FCC
unit-cell volume, then converts the resulting areal flux into a per-unit-cell diffusion rate.
(a)(i) Which end corrodes. In a concentration cell with identical metal at
both electrodes, the electrode facing the more dilute ion solution has a lower
Nernst (reduction) potential, making it the anode: it must dissolve (oxidize, $\text{Cu}\to
\text{Cu}^{2+}+2e^-$) to raise its local ion concentration back toward equilibrium. Here the
$0.002\ M$ end is dilute, so the end in the 0.002 M solution corrodes; the
0.03 M end is the cathode (protected).
(a)(ii) Potential difference. By the Nernst equation applied to each
half-cell and subtracting (the standard potentials cancel since both ends are copper),
$$\Delta E=\frac{0.0592}{n}\log\!\left(\frac{C_{hi}}{C_{lo}}\right)
=\frac{0.0592}{2}\log\!\left(\frac{0.03}{0.002}\right)=\frac{0.0592}{2}\log(15)=\boxed{34.8\ \text{mV}}.$$
(b) Convert atoms-per-unit-cell to a volumetric concentration. FCC unit-cell
volume $V_{cell}=a_0^3=(0.365\times10^{-9})^3=4.865\times10^{-29}\ \text{m}^3$. Surface
concentration
$$c_1=\frac{1\ \text{atom}}{40\,V_{cell}}=5.14\times10^{26}\ \text{atoms/m}^3,$$
and at 2 mm depth
$$c_2=\frac{1\ \text{atom}}{50\,V_{cell}}=4.11\times10^{26}\ \text{atoms/m}^3.$$
Fick's first law flux. With $\Delta x=2\ \text{mm}=2\times10^{-3}$ m,
$$J=D\,\frac{c_1-c_2}{\Delta x}=(3\times10^{-11})\times\frac{(5.14-4.11)\times10^{26}}{2\times10^{-3}}
=1.54\times10^{18}\ \text{atoms/(m}^2\cdot\text{s)}.$$
Convert to atoms per unit cell per minute. The flux is atoms crossing a unit
area per second; scaling by one unit-cell cross-sectional face area $a_0^2$ and then by 60 s/min,
$$\dot n_{cell}=J\,a_0^2\times60=(1.54\times10^{18})\times(0.365\times10^{-9})^2\times60
=\boxed{12.3\ \text{C atoms per unit cell per minute}}.$$