The basic principles of Chapman–Enskog theory can be extended to more diverse physical models, including gas mixtures and molecules with internal degrees of freedom. In the high-density regime, the theory can be adapted to account for collisional transport of momentum and energy, i.e. transport over a molecular diameter
during a collision, rather than over a
mean free path (
in between collisions). Including this mechanism predicts a density dependence of the viscosity at high enough density, which is also observed experimentally. Obtaining the corrections used to account for transport during a collision for soft molecules (i.e.
Lennard-Jones or
Mie molecules) is in general non-trivial, but success has been achieved at applying
Barker-Henderson perturbation theory to accurately describe these effects up to the
critical density of various fluid mixtures. In general circumstances, however, these higher-order corrections may not give reliable improvements to the first-order theory, due to the fact that the Chapman–Enskog expansion does not always converge. (On the other hand, the expansion is thought to be at least asymptotic to solutions of the Boltzmann equation, in which case truncating at low order still gives accurate results.) Even if the higher order corrections do afford improvement in a given system, the interpretation of the corresponding hydrodynamical equations is still debated.
Revised Enskog theory The extension of Chapman–Enskog theory for multicomponent mixtures to elevated densities, in particular, densities at which the
covolume of the mixture is non-negligible was carried out in a series of works by
E. G. D. Cohen and others, and was coined Revised Enskog theory (RET). The successful derivation of RET followed several previous attempt at the same, but which gave results that were shown to be inconsistent with
irreversible thermodynamics. The starting point for developing the RET is a modified form of the Boltzmann Equation for the s-particle velocity distribution function, \left(\frac{\partial}{\partial t} + \mathbf{v}_i \cdot \frac{\partial }{\partial \mathbf{r}} + \frac{\mathbf{F}_i}{m_i}\cdot \frac{\partial}{\partial \mathbf{v}_i}\right)f_i = \sum_j S_{ij}(f_i, f_j) where \mathbf{v}_i(\mathbf{r}, t) is the velocity of particles of species i, at position \mathbf{r} and time t, m_i is the particle mass, \mathbf{F}_i is the external force, and S_{ij}(f_i, f_j) = \iiint \left[g_{ij}(\sigma_{ij} \mathbf{k}) \, f_i'(\mathbf{r}) \, f_j'(\mathbf{r} + \sigma_{ij} \mathbf{k}) - g_{ij}(- \sigma_{ij} \mathbf{k}) \, f_i(\mathbf{r}) \, f_j(\mathbf{r} - \sigma_{ij} \mathbf{k})\right] d \tau The difference in this equation from classical Chapman–Enskog theory lies in the streaming operator S_{ij} , within which the velocity distribution of the two particles are evaluated at different points in space, separated by \sigma_{ij} \mathbf{k} , where \mathbf{k} is the
unit vector along the line connecting the two particles centre of mass. Another significant difference comes from the introduction of the factors g_{ij} , which represent the enhanced probability of collisions due to excluded volume. The classical Chapman–Enskog equations are recovered by setting \sigma_{ij} = 0 and g_{ij}(\sigma_{ij} \mathbf{k}) = 1 . A point of significance for the success of the RET is the choice of the factors g_{ij} , which is interpreted as the
pair distribution function evaluated at the contact distance \sigma_{ij} . An important factor to note here is that in order to obtain results in agreement with
irreversible thermodynamics, the g_{ij} must be treated as functionals of the density fields, rather than as functions of the local density.
Results from Revised Enskog theory One of the first results obtained from RET that deviates from the results from the classical Chapman–Enskog theory is the
Equation of State. While from classical Chapman–Enskog theory the
ideal gas law is recovered, RET developed for rigid elastic spheres yields the pressure equation \frac{p}{nkT} = 1 + \frac{2 \pi n}{3} \sum_i \sum_j x_i x_j \sigma_{ij}^3 g_{ij} , which is consistent with the
Carnahan-Starling Equation of State, and reduces to the ideal gas law in the limit of infinite dilution (i.e. when n \sum_{i,j} x_i x_j \sigma_{ij} ^3 \ll 1 ) For the
transport coefficients:
viscosity,
thermal conductivity,
diffusion and
thermal diffusion, RET provides expressions that exactly reduce to those obtained from classical Chapman–Enskog theory in the limit of infinite dilution. However, RET predicts a density dependence of the
thermal conductivity, which can be expressed as \lambda = (1 + n \alpha_{\lambda}) \lambda_0 + n^2 T^{1 / 2} \lambda_{\sigma} where \alpha_{\lambda} and \lambda_\sigma are relatively weak functions of the composition, temperature and density, and \lambda_0 is the thermal conductivity obtained from classical Chapman–Enskog theory. Similarly, the expression obtained for viscosity can be written as \mu = (1 + n T \alpha_{\mu} ) \mu_0 + n^2 T^{1 / 2} \mu_{\sigma} with \alpha_{\mu} and \mu_{\sigma} weak functions of composition, temperature and density, and \mu_0 the value obtained from classical Chapman–Enskog theory. For
diffusion coefficients and
thermal diffusion coefficients the picture is somewhat more complex. However, one of the major advantages of RET over classical Chapman–Enskog theory is that the dependence of diffusion coefficients on the thermodynamic factors, i.e. the derivatives of the
chemical potentials with respect to composition, is predicted. In addition, RET does not predict a strict dependence of D \sim \frac{1}{n}, \quad D_T \sim \frac{1}{n} for all densities, but rather predicts that the coefficients will decrease more slowly with density at high densities, which is in good agreement with experiments. These modified density dependencies also lead RET to predict a density dependence of the
Soret coefficient, S_T = \frac{D_T}{D}, \quad \left( \frac{\partial S_T}{\partial n} \right)_{T} \neq 0 , while classical Chapman–Enskog theory predicts that the Soret coefficient, like the viscosity and thermal conductivity, is independent of density.
Applications While Revised Enskog theory provides many advantages over classical Chapman–Enskog theory, this comes at the price of being significantly more difficult to apply in practice. While classical Chapman–Enskog theory can be applied to arbitrarily complex spherical potentials, given sufficiently accurate and fast integration routines to evaluate the required
collision integrals, Revised Enskog Theory, in addition to this, requires knowledge of the contact value of the pair distribution function. For mixtures of
hard spheres, this value can be computed without large difficulties, but for more complex intermolecular potentials it is generally non-trivial to obtain. However, some success has been achieved at estimating the contact value of the pair distribution function for
Mie fluids (which consists of particles interacting through a generalised
Lennard-Jones potential) and using these estimates to predict the transport properties of dense gas mixtures and supercritical fluids. Applying RET to particles interacting through realistic potentials also exposes one to the issue of determining a reasonable
"contact diameter" for the soft particles. While these are unambiguously defined for hard spheres, there is still no generally agreed upon value that one should use for the contact diameter of soft particles. ==See also==