The problem involves comparing two diffusive flux scenarios for a binary A-B liquid under steady-state conditions:
We are given the mole fractions of A at two locations, $x_{A1} = 0.8$ and $x_{A2} = 0.1$. The goal is to calculate $\frac{(N_{A1}-N_{A2})}{N_{A1}} \times 100$.
When B is non-diffusing ($N_B=0$), the flux of A ($N_{A1}$) relative to stationary coordinates is given by $N_{A1} = \frac{-D_{AB} C_{total}}{1-x_A} \frac{dx_A}{dz}$. Assuming constant total molar concentration ($C_{total}$), the integrated form over a distance $\Delta z$ is:
$N_{A1} = \frac{D_{AB} C_{total}}{\Delta z} \ln\left(\frac{1-x_{A2}}{1-x_{A1}}\right)$
Substituting the given mole fractions $x_{A1} = 0.8$ and $x_{A2} = 0.1$:
The flux $N_{A1}$ becomes:
$N_{A1} = \frac{D_{AB} C_{total}}{\Delta z} \ln\left(\frac{0.9}{0.2}\right) = \frac{D_{AB} C_{total}}{\Delta z} \ln(4.5)$
Under equimolar counter-diffusion ($N_A + N_B = 0$), the flux of A ($N_{A2}$) relative to stationary coordinates is given by $N_{A2} = -D_{AB} C_{total} \frac{dx_A}{dz}$. The integrated form is:
$N_{A2} = \frac{D_{AB} C_{total}}{\Delta z} (x_{A1} - x_{A2})$
Substituting the given mole fractions $x_{A1} = 0.8$ and $x_{A2} = 0.1$:
$N_{A2} = \frac{D_{AB} C_{total}}{\Delta z} (0.8 - 0.1) = \frac{D_{AB} C_{total}}{\Delta z} (0.7)$
The quantity to compute is $\frac{(N_{A1}-N_{A2})}{N_{A1}} \times 100$. This can be rewritten as:
$\left(1 - \frac{N_{A2}}{N_{A1}}\right) \times 100$
Let $K = \frac{D_{AB} C_{total}}{\Delta z}$ for simplicity. The ratio of the fluxes is:
$\frac{N_{A2}}{N_{A1}} = \frac{K \times 0.7}{K \times \ln(4.5)} = \frac{0.7}{\ln(4.5)}$
Using the approximate value $\ln(4.5) \approx 1.504077$:
$\frac{N_{A2}}{N_{A1}} \approx \frac{0.7}{1.504077} \approx 0.46540$
Now, calculate the required percentage difference:
$\left(1 - 0.46540\right) \times 100 = 0.53460 \times 100 = 53.460\%$
Rounding the result to one decimal place gives $53.5\%$.
Consider a non-reactive binary mixture of two ideal gases A and B in an isothermal horizontal closed tube. Due to the concentration difference at the two ends of the tube, equimolal counterdiffusion occurs along the axial direction. No concentration gradients exist in the radial direction. The profile for partial pressure of component A ($p_A$) as a function of axial distance $z$ is shown in the figure. The partial pressure of component B ($p_B$) approaches zero at $z = 0.8 \text{ m}$. At a location $z = z_1$ the partial pressures of the components A and B are equal. The value of $z_1$ (in m) is _____ (rounded off to two decimal places).
