Mass diffusivity
Diffusivity, mass diffusivity or diffusion coefficient is usually written as the proportionality constant between the molar flux due to molecular diffusion and the negative value of the gradient in the concentration of the species. More accurately, the diffusion coefficient times the local concentration is the proportionality constant between the negative value of the mole fraction gradient and the molar flux. This distinction is especially significant in gaseous systems with strong temperature gradients. Diffusivity derives its definition from Fick's law and plays a role in numerous other equations of physical chemistry.
The diffusivity is generally prescribed for a given pair of species and pairwise for a multi-species system. The higher the diffusivity, the faster they diffuse into each other. Typically, a compound's diffusion coefficient is ~10,000× as great in air as in water. Carbon dioxide in air has a diffusion coefficient of 16 mm2/s, and in water its diffusion coefficient is 0.0016 mm2/s.
Diffusivity has dimensions of length2 / time, or m2/s in SI units and cm2/s in CGS units.
Temperature dependence of the diffusion coefficient
Solids
The diffusion coefficient in solids at different temperatures is generally found to be well predicted by the Arrhenius equation:where
- D is the diffusion coefficient,
- D0 is the maximal diffusion coefficient,
- EA is the activation energy for diffusion,
- T is the absolute temperature,
- R ≈ 8.31446J/ is the universal gas constant.
Liquids
An approximate dependence of the diffusion coefficient on temperature in liquids can often be found using Stokes–Einstein equation, which predicts thatwhere
- D is the diffusion coefficient,
- T1 and T2 are the corresponding absolute temperatures,
- μ is the dynamic viscosity of the solvent.
Gases
The dependence of the diffusion coefficient on temperature for gases can be expressed using Chapman–Enskog theory :where
- D is the diffusion coefficient,
- A is approximately
- 1 and 2 index the two kinds of molecules present in the gaseous mixture,
- T is the absolute temperature,
- M is the molar mass,
- p is the pressure,
- is the average collision diameter ,
- Ω is a temperature-dependent collision integral .
is obtained when inserting the ideal gas law into the expression obtained directly from Chapman-Enskog theory, which may be written as
where is the molar density of the gas, and
with the universal gas constant. At moderate densities this simple relation no longer holds, and one must resort to Revised Enskog Theory. Revised Enskog Theory predicts a diffusion coefficient that decreases somewhat more rapidly with density, and which to a first approximation may be written as
where is the radial distribution function evaluated at the contact diameter of the particles. For molecules behaving like hard, elastic spheres, this value can be computed from the Carnahan-Starling Equation, while for more realistic intermolecular potentials such as the Mie potential or Lennard-Jones potential, its computation is more complex, and may involve invoking a thermodynamic perturbation theory, such as SAFT.
Pressure dependence of the diffusion coefficient
For self-diffusion in gases at two different pressures, the following empirical equation has been suggested:where
- D is the diffusion coefficient,
- ρ is the gas mass density,
- P1 and P2 are the corresponding pressures.
Population dynamics: dependence of the diffusion coefficient on fitness
where is constant and r depends on population densities and abiotic characteristics of the living conditions. This dependence is a formalisation of the simple rule: Animals stay longer in good conditions and leave quicker bad conditions.
Effective diffusivity in porous media
The effective diffusion coefficient describes diffusion through the pore space of porous media. It is macroscopic in nature, because it is not individual pores but the entire pore space that needs to be considered. The effective diffusion coefficient for transport through the pores, De, is estimated as follows:where
- D is the diffusion coefficient in gas or liquid filling the pores,
- εt is the porosity available for the transport,
- δ is the constrictivity,
- τ is the tortuosity.