Page 46 - Modelling in Transport Phenomena A Conceptual Approach
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2.4.  TOTAL FLUX                                                     27


              When air is pumped through a pipe, it is considered to be a single phase and
           a  single component system.  In this  case, there is  no  ambiguity in  defining the
           characteristic velocity.  However, if  the oxygen in the air were reacting,  then the
           fact that air is composed predominantly of two species, 02 and Na, had to be taken
           into account.  Hence, air should be considered a single phase, binary  component
           system. For a single phase system composed of n components, the general definition
           of  a characteristic velocity is given by
                                               n
                                                                             (2.3-2)
                                               a
           where pi is the weighting factor and vi is the velocity of  a constituent.  The three
           most common characteristic velocities are listed in Table 2.2. The term vi in the
           definition of  the volume average velocity represents the partial molar volume of  a
           constituent.  The molar  average velocity is equal to the volume average velocity
           when the total molar concentration, c,  is constant.  On the other hand, the mass
           average velocity is equal to the voIume average velocity when the total mass density,
           p, is constant.


           Table 2.2  Common characteristic velocities.
            Characteristic Velocity   Weighting Factor    Formulation
            Mass average           Mass fraction (wi)    21 = xi w;v;
            Molar average          Mole fraction (xi)    v* = xi xivi

            Volume average         Volume fraction (ciVi)  v'   = xi ciVivi

              The choice of  a characteristic velocity is arbitrary.  For a given problem, it is
           more convenient to select a characteristic velocity which will make the convective
           flux zero and thus yield a simpler problem.  In the literature, it is common practice
           to use the molar average velocity for dilute gases, i.e., c = constant, and the mass
           average velocity for liquids, i.e., p = constant.
              It should be noted that  the molecular mass flux expression given by  Eq.  (2.1-
           6) represents the molecular mass flux with  respect  to the mass average velocity.
           Therefore, in the equation representing the total mass flux, the characteristic ve
           locity in the convective mass flux term is taken as the mass average velocity.  On
           the other hand,  Q. (2.1-8) is the molecular molar flux with respect  to the mw
           lar average velocity.  Therefore, the molar average velocity is considered to be the
           characteristic velocity in the convective molar flux term.


           2.4  TOTAL FLUX

           Since the total flux of  any  quantity  is the sum of  its molecular  and convective
           fluxes, then
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