Past exam of the MPhil in micro- and nanotechnology enterprise course of the University of Cambridge 2017 Paper 1 Section B 11 ii Solution Created 2026-10-20 Updated 2026-10-20
On the stated area, the total electric current is . The known ohmic polarization is . Applying the supplied anodic Tafel equation givesAssume the quoted limiting current uses the same cathodic area convention. A steady diffusion-film model gives . The Nernst equation then makes the cathodic concentration overpotential magnitudeRelative to the local surface equilibrium potential, the cathode also needs an activation overpotential. Neglecting anodic concentration polarization, the separated-loss accounting isTo calculate that activation term, adopt a single effective two-electron Butler-Volmer equation with constant transfer coefficients satisfying , no anodic concentration polarization and reduction proportional to the surface concentration. The supplied anodic Tafel slope then determines the reverse slope throughWith and cathodic overpotential referenced to bulk equilibrium,Solving at gives , including both concentration and activation effects. ThusThe V concentration loss must not be added again. The kinetic assumption matters: the supplied slope is for copper oxidation, and an exchange current density alone does not specify every cathodic current-potential relation. A multistep copper reaction need not obey the effective single-step relation used for this estimate.
At fixed discharge current, delivered voltage can be represented aswhere is discharged charge and the terms denote distinct physical losses. A typical trace has an initial drop from open circuit, an approximately flat useful region and a final decline toward cutoff. Its exact shape depends on the cell chemistry and current; not every battery has an equally flat plateau.
Four distinguishable contributions are:
- Ohmic polarization: electronic, ionic and contact resistance cause a rapid drop on applying current. This need not wait for a concentration gradient to develop.
- Activation overpotential: finite electrode-reaction kinetics require a departure from equilibrium to sustain charge transfer. It is important when the exchange current is small.
- Concentration overpotential: electrolyte transport and diffusion within active particles can deplete reactants or accumulate products near reaction sites. These losses often grow near the end of discharge or at high current.
- Phase-transformation polarization: nucleation and growth of a new phase can require extra driving force, produce an initial voltage dip or cause hysteresis. It is especially relevant to conversion and two-phase electrodes, rather than a universal independent loss in every chemistry.
Terminology sometimes groups solid-state transport or phase-change effects differently. The important distinction is the mechanism, not counting the same diffusion loss under two names. A falling equilibrium voltage as composition changes is also not, by itself, polarization.
An illustrative discharge voltage combines equilibrium changes and distinct losses
. Original stipulated model, not battery measurements. The loss components show an instantaneous resistive contribution, activation loss, a transient nucleation-related contribution and increasing late-discharge transport loss. The equilibrium curve is plotted separately. Details.