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• a good agreem<strong>en</strong>t has be<strong>en</strong> found betwe<strong>en</strong> macro-scale resolutions and micro-<br />
scale, direct simulations, which validates the proposed theoretical mo<strong>de</strong>l,<br />
• thermal diffusion modifies the local conc<strong>en</strong>tration and this modification <strong>de</strong>p<strong>en</strong>ds<br />
locally on the porosity, thermal conductivity ratio and fluid velocity. Therefore, we<br />
cannot ignore this effect.<br />
A new experim<strong>en</strong>tal setup has be<strong>en</strong> <strong>de</strong>signed and ma<strong>de</strong>-up to <strong>de</strong>termine directly the<br />
effective diffusion and thermal diffusion coeffici<strong>en</strong>ts for binary mixtures. This setup is a<br />
closed system, which helped carry out the experim<strong>en</strong>ts for the case of pure diffusion only.<br />
The experim<strong>en</strong>ts have be<strong>en</strong> performed with special all-glass two-bulb apparatus,<br />
containing two double-spherical layers. The diffusion and thermal diffusion of heliumnitrog<strong>en</strong><br />
and helium-carbon dioxi<strong>de</strong> systems through cylindrical samples first without<br />
porous media and th<strong>en</strong> filled with spheres of differ<strong>en</strong>t diameters and thermal conductivities<br />
were measured at the atmospheric pressure. Conc<strong>en</strong>trations were <strong>de</strong>termined by analysing<br />
the gas mixture composition in the bulbs with a katharometer <strong>de</strong>vice. A transi<strong>en</strong>t-state<br />
method for coupled evaluation of thermal diffusion and Fick coeffici<strong>en</strong>t in two bulbs<br />
systems has be<strong>en</strong> proposed. Here, with a simple thermal diffusion experim<strong>en</strong>t, this mo<strong>de</strong>l<br />
is able to <strong>de</strong>termine both diffusion and thermal diffusion coeffici<strong>en</strong>ts. The <strong>de</strong>termination of<br />
diffusion and thermal diffusion coeffici<strong>en</strong>ts is done by a curve fitting of the temporal<br />
experim<strong>en</strong>tal results with the transi<strong>en</strong>t-state solution <strong>de</strong>scribing the mass balance betwe<strong>en</strong><br />
the two bulbs. The results showed<br />
• a <strong>de</strong>p<strong>en</strong>d<strong>en</strong>cy of the thermal diffusion and diffusion coeffici<strong>en</strong>ts on the porosity,<br />
• a good agreem<strong>en</strong>t with theoretical results, which confirm the validity of the<br />
theoretical results for pure diffusion,<br />
• the tortuosity of the medium calculated using both effective diffusion and effective<br />
thermal diffusion coeffici<strong>en</strong>ts were not differ<strong>en</strong>t to the measurem<strong>en</strong>t accuracy,<br />
• the experim<strong>en</strong>tal results also showed that the particle-particle touching has not a<br />
significant influ<strong>en</strong>ce on the effective thermal diffusion coeffici<strong>en</strong>ts.<br />
There is still much work to be done concerning thermal diffusion in porous media. Several<br />
perspectives can be proposed. The following ones pres<strong>en</strong>t especial interest<br />
• in the theoretical part of this study we <strong>de</strong>veloped a coupled heat and mass transfer<br />
macro-scale equation with a non-thermal equilibrium case (using a two-equation<br />
temperature problem). One may use this mo<strong>de</strong>l wh<strong>en</strong> the assumption of thermal<br />
equilibrium is not valid. However, the closure problems have not be<strong>en</strong> solved for<br />
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