Page 248 - gas transport in porous media
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CHAPTER 14

                           EXPERIMENTAL DETERMINATION OF TRANSPORT
                           PARAMETERS





                           OLGA ŠOLCOVÁ AND PETR SCHNEIDER
                           Institute of Chemical Process Fundamentals, Czech Academy of Science, Rozvojová 135, 165 02 Praha
                           6, Czech Republic


                           Any prediction or simulation of gas transport in porous solids is based on mass
                           balances. The balance equations incorporate inevitably constitutive equations, which
                           relate the intensity of mass flux to mass flux driving forces. Constitutive equations
                           comprise information of three kinds:
                           1. Properties of components of the gas mixture: bulk diffusion coefficients of all pairs
                              of components of the gas mixture, component viscosities and their mean speeds.
                              Such properties are, usually, readily available.
                           2. The physical laws, which describe the gas transport, with idealized units of
                              the porous medium. Usually, cylindrical capillaries are utilized because of the
                              availability and simplicity of the laws.
                           3. Characteristics of the porous medium. Since the diverse complicated nature of the
                              porous medium is usually unknown it must be modeled. Modeling of the porous
                              structure is based on units from paragraph 2 and accounts for pore-size distribu-
                              tion and other factors not apprehended by pore units. Today two basic models are
                              available for description of combined (diffusion and permeation) transport of mul-
                              ticomponent gas mixtures: the Mean Transport-Pore Model (MTPM) (Fott et al.,
                              1983; Schneider and Gelbin, 1984) and the Dusty Gas Model (DGM) (Jackson,
                              1977; Mason and Malinauskas, 1983).
                             Mean Transport-Pore Model (MTPM) assumes that the decisive part of the gas
                           transport takes place in transport-pores that are visualized as cylindrical capillaries
                           with radii distributed around the mean value  r  (first model parameter). The width of
                           this distribution is characterized by the mean value of the squared transport-pore radii,
                             2
                            r   (second model parameter). The third model parameter is the ratio of porosity, ε t ,
                                                                (Schneider, 1978; Novák et al., 1988).
                           and tortuosity of transport-pores, q t , ψ = ε t/q t


                                                           245
                           C. Ho and S. Webb (eds.), Gas Transport in Porous Media, 245–272.
                           © 2006 Springer.
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