1994
DOI: 10.1007/978-3-540-48650-3
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Multicomponent Transport Algorithms

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Cited by 247 publications
(248 citation statements)
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“…The methodology treats the fluid as a mixture of perfect gases. We use a mixture-averaged model for differential species diffusion (see [28] for complete discussion of this approximation) and ignore Soret, Dufour, gravity and radiative transport processes. With these assumptions, the low Mach number equations for an open domain are ∂ρU ∂t…”
Section: Computational Methodologymentioning
confidence: 99%
“…The methodology treats the fluid as a mixture of perfect gases. We use a mixture-averaged model for differential species diffusion (see [28] for complete discussion of this approximation) and ignore Soret, Dufour, gravity and radiative transport processes. With these assumptions, the low Mach number equations for an open domain are ∂ρU ∂t…”
Section: Computational Methodologymentioning
confidence: 99%
“…When there are several modes for internal energy and/or several species present in the mixture, the above simple expression is replaced by the solution of a linear system leading finally to the volume viscosity [12]. Within the approximation of Monchick and Mason, neglecting complex collisions with more than one quantum jump, the reduced system is diagonal and typically yields κ by [4]:…”
Section: Volume and Shear Viscositymentioning
confidence: 99%
“…The higher the value of m, the more expensive the underlying algorithm and the more accurate the expression for κ, hence our choice of m = 6. The simplest and cheapest of the models, m = 2 (EGSK2()) considers only the transport system matrix associated with the internal energy, whereas m = 6 (EGSK6()) corresponds to solving the matrix system associated with both translational and internal energy and relies on temperaturedependent ratios of collision integrals, which are evaluated as discussed in [12,13,54]. At the end, a direct inversion is performed to evaluate the volume viscosity for a given state of the mixture, characterized by the temperature and species mass fractions.…”
Section: Volume and Shear Viscositymentioning
confidence: 99%
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“…where D m is the mixture-averaged diffusion coefficient for species m; q is the local fluid mass density, and X m is the species mole frac- [26] for a detailed derivation and justification of this approximation).…”
Section: Numerical Simulationmentioning
confidence: 99%