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Thermal conductivity Maxwell equation

The temperature fields induced by microwave heating can be modeled via the simultaneous solution of Maxwell s equations (for the electromagnetic component of the problem) and the heat equation. The modeling is very challenging, in part because the dielectric constants sj. and s" are functions of temperature and the microwave frequency as well as of the microstructural and chemical details of the ceramic [Eq. (lb)]. Also, the thermal conductivity, k (which is needed for the heat transfer calculations), typically is a function of temperature as well as of microstructural variables such as porosity. ... [Pg.1690]

A consequence of the complex interplay of the dielectric and thermal properties with the imposed microwave field is that both Maxwell s equations and the Fourier heat equation are mathematically nonlinear (i.e., they are in general nonlinear partial differential equations). Although analytical solutions have been proposed under particular assumptions, most often microwave heating is modeled numerically via methods such as finite difference time domain (FDTD) techniques. Both the analytical and the numerical solutions presume that the numerical values of the dielectric constants and the thermal conductivity are known over the temperature, microstructural, and chemical composition range of interest, but it is rare in practice to have such complete databases on the pertinent material properties. [Pg.1690]

For 1-D steady-state heat conduction, the joined materials form a series thermal circuit with an effective resistance, Reff = X(Ax,/K,), where Ax, and K, are the thickness and the thermal conductivity, respectively, of the i layer. Figure 8 shows the projected thermal resistance of ZS/Cu-clad-Mo joints made using the four brazes as a function of % clad layer thickness. This figure also shows the thermal resistance of the ZS composite and Cu-clad-Mo of the same total thickness (5.1 mm) as the joined assembly. For calculation Axzs= Axa,.Mo= 0.25x10 m, Axticusi1 = 100x1 o m, and K of Cu-clad-Mo with different Cu layer thicknesses is from ref . The conductivity of ZS (Kzs) is calculated from the Maxwell equation for spherical particles... [Pg.512]

The temperature distribution in a long cylindrical steady-state thermal plasma colunm stabilized by walls in a tube of radius R is described by the Elenbaas-Heller equation, assuming heat transfer across the positive coliunn provided by heat conduction with the coefficient X(T). According to a Maxwell equation, cur IE = 0 and the electric field in a long homogeneous arc colunm is constant across its cross section. Radial distributions... [Pg.193]

An extra property very used to characterize the MPCM and PCS is the thermal conductivity. It is calculated in different manners, as Youssef et al. ° reported in a review. One mode to calculate it is by Maxwell s ° relation e q)ressed in Equation 62.5, where mpcm is represented as the thermal omduclivity of the miaocapsule, comis the thermal conductivity of the content, and c pcm is the volume liacliMi of the MPCM ... [Pg.1469]

Maxwell s (1904) equation for electrical conductivity may be used to predict thermal conductivity as follows ... [Pg.421]

Figure 12.30. Comparison of experimental and predicted thermal conductivities for glass-sphere-filled polymers. The upper curves are for polyethylene, the lower curves for polystyrene. Except for Kerner equation plot ( ), curves and data are from Sundstrom and Chen (1970). (--) Maxwell (—) Cheng-Vachon (- -) Behrens and Peterson-Hermans. (From Sundstrom, D. W., and Chen, S. Y., 1970, J. Compos. Mater. 4, 113 courtesy Technomic Publishing Co.)... Figure 12.30. Comparison of experimental and predicted thermal conductivities for glass-sphere-filled polymers. The upper curves are for polyethylene, the lower curves for polystyrene. Except for Kerner equation plot ( ), curves and data are from Sundstrom and Chen (1970). (--) Maxwell (—) Cheng-Vachon (- -) Behrens and Peterson-Hermans. (From Sundstrom, D. W., and Chen, S. Y., 1970, J. Compos. Mater. 4, 113 courtesy Technomic Publishing Co.)...
The ordinary kinetics theory of neuter gas, the Boltzmann equation is considered with collision term for binary collisions and is despised the body s force F . This simplified Boltzmann equations is an integro - differential non lineal equation, and its solution is very complicated for solve practical problems of fluids. However, Boltzmann equation is used in two important aspects of dynamic fluids. First the fundamental mechanic fluids equation of point of view microscopic can be derivate of Boltzmann equation. By a first approximation could obtain the Navier-Stokes equations starting from Boltzmann equation. The second the Boltzmann equation can bring information about transport coefficient, like viscosity, diffusion and thermal conductivity coefficients (Pai, 1981 Maxwell, 1997). [Pg.78]

The macropore diffusion of nc adsorbates is described by the Maxwell-Stefan equation as learnt in Chapter 8 (Section 8.8). The micropore diffusion in crystal is activated and is described by eq. (10.6-11), and the adsorption process at the micropore mouth is assumed to be very fast compared to diffusion so that local equilibrium is established at the mouth. Adsorption and desorption of adsorbates are associated with heat release which in turn causes a rise or drop in temperature of the pellet. We shall assume that the thermal conductivity of the pellet is large such that the pellet temperature is uniform and all the heat transfer resistance is located at the thin film surrounding the pellet. How large the pellet temperature will change during the course of adsorption depends on the interplay between the rate of adsorption, the heat of adsorption and the rate of heat dissipation to the surrounding. But the rate of adsorption at any given time depends on the temperature. Thus the mass and heat balances are coupled and therefore their balance equations must be solved simultaneously for the proper description of concentration and temperature evolution. [Pg.676]

The Agari-Uno model (Agari and Uno 1986) shows that the thermal conductivity data are deviating from the Maxwell-Eucken equation at about a 10% volumetric fraction. At a high filler volume, the measured value was much higher than the prediction using existing correlations. This approach is based on series and parallel models and considers the crystaUmity of both phases and interfacial factor A, as shown in equation (11.5) ... [Pg.197]

The formalism employed for permeabihty relationships in the this section, such as the series model, parallel model. Maxwell s equation, and the equivalent box model (EBM) can be employed for thermal conductivity by replacing P with K. [Pg.364]

In his famous book on quantum mechanics, Dirac stated that chemistry can be reduced to problems in quantum mechanics. It is true that many aspects of chemistry depend on quantum mechanical formulations. Nevertheless, there is a basic difference. Quantmn mechanics, in its orthodox form, corresponds to a deterministic time-reversible description. This is not so for chemistry. Chemical reactions correspond to irreversible processes creating entropy. That is, of course, a very basic aspect of chemistry, which shows that it is not reducible to classical dynamics or quantum mechanics. Chemical reactions belong to the same category as transport processes, viscosity, and thermal conductivity, which are all related to irreversible processes.. .. [A]s far back as in 1870 Maxwell considered the kinetic equations in chemistry, as well as the kinetic equations in the kinetic theory of gases, as incomplete dynamics. From his point of view, kinetic equations for... [Pg.173]

Thermal conductivity data for mixtures of solids have been correlated [62] using Maxwell s [63] equation ... [Pg.160]


See other pages where Thermal conductivity Maxwell equation is mentioned: [Pg.11]    [Pg.85]    [Pg.502]    [Pg.291]    [Pg.262]    [Pg.274]    [Pg.664]    [Pg.305]    [Pg.262]    [Pg.2247]    [Pg.197]    [Pg.91]    [Pg.229]    [Pg.188]    [Pg.48]    [Pg.539]    [Pg.69]   


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