The governing equations for diffusion mass transfer are [35]
\boldsymbol{ j}_A = - \rho \boldsymbol{D}_{AB}\nabla m_A | (367) |
and
\nabla \cdot \boldsymbol{ j}_A + \dot{n_A} = \frac{\partial \rho_A}{\partial t}, | (368) |
where
m_A = \frac{\rho_A}{\rho_A + \rho_B} | (369) |
and
\rho = \rho_A + \rho_B. | (370) |
In these equations \boldsymbol{j}_A is the mass flux of species A, \boldsymbol{D}_{AB} is the mass diffusivity, m_A is the mass fraction of species A and \rho_A is the density of species A. Furthermore, \dot{n_A} is the rate of increase of the mass of species A per unit volume of the mixture. Another way of formulating this is:
\boldsymbol{ J}_A^* = - C \boldsymbol{D}_{AB}\nabla x_A | (371) |
and
\nabla \cdot \boldsymbol{ J}_A^* + \dot{N_A} = \frac{\partial C_A}{\partial t}. | (372) |
where
x_A = \frac{C_A}{C_A + C_B} | (373) |
and
C = C_A + C_B. | (374) |
Here, \boldsymbol{J}_A^* is the molar flux of species A, \boldsymbol{D}_{AB} is the mass diffusivity, x_A is the mole fraction of species A and C_A is the molar concentration of species A. Furthermore, \dot{N_A} is the rate of increase of the molar concentration of species A.
The resulting equation now reads
\nabla \cdot (- \rho \boldsymbol{ D}_{AB} \cdot \nabla m_A)+ \frac{\partial \rho_A}{\partial t} = \dot{n_A} . | (375) |
or
\nabla \cdot (- C \boldsymbol{ D}_{AB} \cdot \nabla x_A)+ \frac{\partial C_A}{\partial t} = \dot{N_A} . | (376) |
If C and \rho are constant, these equations reduce to:
\nabla \cdot (- \boldsymbol{ D}_{AB} \cdot \nabla \rho_A)+ \frac{\partial \rho_A}{\partial t} = \dot{n_A} . | (377) |
or
\nabla \cdot (- \boldsymbol{ D}_{AB} \cdot \nabla C_A)+ \frac{\partial C_A}{\partial t} = \dot{N_A} . | (378) |
Accordingly,
by comparison with the heat equation, the correspondence in Table
() arises.