Neither end allows ions through
Two plates have full separation , with position increasing rightward and initially uniform ion densities. Apply electrode potentials and . Here is the total voltage divided by thermal voltage. Both ionic fluxes vanish at both ends.
Cations first move left and anions right. Cations accumulate and anions deplete near the left plate, with the reverse near the right plate. Diffusion increasingly opposes migration and accumulated charge screens the interior field. Each species keeps its total particle number throughout this closed-cell process.
Reading: Bazant
Calculate charge and current from the profiles
Gauss’s law gives metal charge per area from the electric field normal to the surface and directed into solution. This normal points rightward at the left plate and leftward at the right plate, giving the opposite signs below. Surface charge density is in .
The external circuit changes electronic charge in the metal, so external current is the electrode-charge derivative with respect to dimensional time . Ionic current within solution can vary with position as space charge changes. Adding displacement current gives a spatially uniform total current in one dimension.
Reading: Bazant · MIT 10.626
A small surface potential decays exponentially
Setting the equilibrium fluxes to zero gives Boltzmann distributions. If local potential relative to the bulk is small compared with thermal voltage, retain the first-order term in each exponential. Charge density becomes proportional to potential. Poisson’s equation then reduces to a linear equation, the Debye–Hückel approximation.
Near a single surface far from the other plate, potential decays from surface value over a Debye length. Its surface slope gives a charge proportional to voltage. The differential capacitance per area is permittivity divided by Debye length. A short charge separation produces a large capacitance.
Reading: MIT 10.626 · Bazant
The charging time combines two lengths
The bulk resistance supplies ions to thin surface layers. A uniform monovalent electrolyte has conductivity . Area-specific bulk resistance, meaning resistance multiplied by cross-sectional area, is full gap divided by conductivity and has units of ohm square metres. The two equal double-layer capacitors are in series, halving the capacitance.
Multiply resistance by the series capacitance to obtain charging time. It lies between diffusion across the double layer and diffusion across the whole cell. The factor two comes from using a full gap and two equal layers; a half-gap convention expresses the same result differently.
Reading: Bazant · MIT 10.626
Work a charging example
For , and , charging takes . The layer diffusion time is and whole-cell diffusion time is . Each has units of time but describes a different transport distance.
With and total voltage , each final layer takes about half the voltage. The right electrode approaches . The table is an analytic thin-layer, linear-circuit reference. A PNP solution should approach it in that limit.
| 0.5 | 0.393 | 0.607 |
| 1.0 | 0.632 | 0.368 |
| 2.0 | 0.865 | 0.135 |
| 3.0 | 0.950 | 0.0498 |
Larger voltages require the ion distributions
A larger surface potential adsorbs more neutral salt, reducing bulk concentration and changing differential capacitance. Charging then has several time scales. A numerical calculation must resolve both thin charge layers and slower salt diffusion, conserve ions, keep concentrations positive and approach a stable result under spatial and temporal refinement.
At high surface concentrations, a point-ion model also neglects finite ion size, activity and solvent structure. Increasing voltage calls for a fresh assessment of these effects before extending the model.