1.2 Fluid Mass Fraction Conservation
The mass fraction of each fluid, or its "presence probability", mk, in a multi-fluid population is assumed to be a conserved quantity. Its value at each point in the flow domain is computed by PHOENICS through solution of the following conservation equations of conventional type:
d(rmk)/dt+ div(rVmk- Gt grad mk ) = Rm,k
Rm,k, the net rate of k-fluid generation, is the balance of micromixing rate, Rmix,k, and interphase transfer, Sp,k:
Rm,k = Rmix,k + Sp,k
The source term, Sp,k, is due solely to transfer of mass into the gas phase from reacting particles (e.g. coal). In all other cases there are no such a source.
The term, Rmix,k, is resulting from micromixing of the fluids as they move past, or collide with, each other in their turbulent motion. It is expressed, for uniformly-divided population, as:
Rmix,k = r Si Sj Fk,i,j mimj Ti,j
wherein:
Ti,j = Cmixe/K
with K standing for the kinetic energy of turbulence, e for its dissipation rate and Cmix for an empirical constant.
The fractional loss of mass is computed by following rules:
       Fk,i,j   = -0.5       for k=i or k=j  and j greater than i+1,
               =  0.0       for k less than i or k greater than j
                            or  j=i+1,
               =  1/(j-i-1) for all other values of i, j and k.
The sources that resulting from the above scheme applied to the interactions between,say, the 5 fluids with T=r=1,would be in fact as follows:
   Rmix,1=-0.5(m3+
                            m4+
                            m5)m1
   Rmix,2= m1m3+
                  m1m4/2+
                  m1m5/3-
                  0.5(m4+
                            m5)m2
   Rmix,3=                                     m4(m1/2+m2)+
   m5(m1/3+m2/2)-
                  0.5(m1+
   m5)m3
   Rmix,4=
   m3m5+
   m2m5/2+
   m1m5/3-
                  0.5(m1+
   m2)m4
   Rmix,5=-0.5(m1+
   m2+
   m3)m5