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Thermal conductivity Chapman-Enskog

Since the forms of the Chapman-Enskog expressions for dilute-gas viscosity and conductivity are so similar, it might be expected that there is a simple relationship between thermal conductivity and viscosity. Indeed, for monatomic gases, combining Eqs. 3.41 and 3.136 yields... [Pg.99]

Chapman-Enskog theory provides the basis for the multicomponent transport properties laid out by Hirschfelder, Curtiss, and Bird [178] and by Dixon-Lewis [103]. The multi-component diffusion coefficients, thermal conductivities, and thermal diffusion coefficients are computed from the solution of a system of equations defined by the L matrix [103], seen below. It is convenient to refer to the L matrix in terms of its nine block submatrices, and in this form the system is given by... [Pg.519]

Evaluate the Chapman-Enskog expression for the thermal conductivity, Eq. 12.87, for the special case of a hard-sphere interaction. Show that for a pure-species, this gives the result cited earlier as Eq. 12.57. [Pg.534]

Equation (2.71) can be compared with Eq. (2.46) for the thermal conductivity of gases, and with Eq. (2.19) for the viscosity. For binary gas mixtures at low pressure, is inversely proportional to the pressure, increases with increasing temperature, and is almost independent of the composition for a given gas pair. For an ideal gas law P = cRT, and the Chapman-Enskog kinetic theory yields the binary diffusivity for systems at low density... [Pg.76]

Estimate the viscosity and thermal conductivity of carbon monoxide using the Chapman-Enskog model at 1 atm... [Pg.92]

Estimate the viscosity and thermal conductivity of carbon dioxide using the Chapman-Enskog model at 1 atm and 250,300, and 400K and compare with the experimental values (Welty et al. (1984)) in the table below ... [Pg.93]

The exact form of the expressions for the diffusional fluxes jj depends on the degree of sophistication used in representing the transport phenomena. A precise approach, including also the calculation of the thermal conductivity of gas mixtures, and based on the Chapman-Enskog kinetic theory, has been described by Dixon-Lewis [122]. However, simpler approaches involving the form j = —pDiAwijAy may also give satisfactory representation in many cases [119—121,123]. [Pg.77]

Using the theory developed by Chapman-Enskog (see Ref. 14), a hierarchy of continuum fluid mechanics formulations may be derived from the Boltzmann equation as perturbations to the Maxwellian velocity distribution function. The first three equation sets are well known (1) the Euler equations, in which the velocity distribution is exactly the Maxwellian form (2) the Navier-Stokes equations, which represent a small deviation from Maxwellian and rely on linear expressions for viscosity and thermal conductivity and (3) the Burnett equations, which include second order derivatives for viscosity and thermal conductivity. [Pg.85]

Gas transport properties are required to apply the theory given in Sections 3.3 and 3.4. Viscosities of pure nonpolar gases at low pressures are predicted from the Chapman-Enskog kinetic theory with a Lennard-Jones 12-6 potential. The collision integrals for viscosity and thermal conductivity with this potential are computed from the accurate curve-fits given by Neufeld et al. (1972). [Pg.59]

The transport coefficients like viscosity, thermal conductivity and self-diffusivity for a pure mono-atomic gas and the diffusivity for binary mixtures obtained from the rigorous Chapman-Enskog kinetic theory with the Lennard-Jones interaction model yield (e.g., [39], sect 8.2 [5], sects 1-4, 9-3 and 17-3) ... [Pg.317]

The difference in the thermal conductivity of the mixture (Ha-He) and pure demonstrating the qualitative agreement between predictions of the Chapman-Enskog theory and chromatograph observations. [Pg.436]

As in the case of the diffusion coefficient, the thermal conductivity in fluids can be predicted with satisfactory accuracy using theoretical expressions, such as the formulas of Chapman and Enskog for monoatomic gases, of Eucken for polyatomic ones, or of Bridgman for pure liquids. The thermal conductivity of solids, however, has not yet been predicted using basic thermophysical or molecular properties, just like the analogous diffusion coefficient. Usually, the... [Pg.88]

The first-order Chapman-Enskog solution of the Boltzmann equation for the viscosity and thermal conductivity of monatomic species are given by the expressions in terms of effective collision cross sections outlined in Chapter 4. However, in order to be consistent with the original papers, here the equivalent expressions in terms of collision integrals are adopted. [Pg.403]

This is the proof of the variational principle that Eq. 93 gives the solution of the Chapman-Enskog equation. The variational principle given in the form of Eq. 93 is much more convenient for practical purposes, because we need not consider restrictions other than simple ones such as the auxiliary conditions, Eqs. 70, 71, and 72. In the case of thermal conduction in a simple gas, Eq. 93 reduces to... [Pg.288]

HeXe mixture recommendation - Chapman and Enskog rigorous kinetic theory (first order for viscosity, third order for thermal conductivity)... [Pg.434]

Chapman (DIPPR) uses the Chapman and Enskog mixture method for calculating thermal conductivity (Hirschfelder, Curtiss, and Bird, 1954) with higher order correction factors given by Kestin (Kestin et al, 1984) and Singh (Singh, Dham, and Gupta, 1992). [Pg.447]


See other pages where Thermal conductivity Chapman-Enskog is mentioned: [Pg.11]    [Pg.105]    [Pg.488]    [Pg.513]    [Pg.73]    [Pg.436]    [Pg.47]    [Pg.95]    [Pg.114]    [Pg.114]    [Pg.101]    [Pg.152]    [Pg.254]    [Pg.408]    [Pg.31]   
See also in sourсe #XX -- [ Pg.99 , Pg.513 ]




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