Step 1: Physical principle for equimolal counterdiffusion.
In equimolal counterdiffusion, the molar flux of A is equal and opposite to the molar flux of B (\(N_A = -N_B\)), so there is no net bulk molar flow. For an ideal gas mixture at constant temperature and steady state, this means the total pressure \(P = p_A + p_B\) is constant at every axial location \(z\), and each partial pressure varies linearly with \(z\), consistent with the straight line shown in the figure.
Step 2: Read the linear profile of \(p_A\) from the figure.
The graph shows \(p_A = 0.6\) bar at \(z = 0\) and the line rises linearly, passing through \(p_A = 1.1\) bar at \(z = 0.2\) m and \(p_A = 1.6\) bar at \(z = 0.4\) m.
Slope \(= \dfrac{1.6-0.6}{0.4-0} = \dfrac{1.0}{0.4} = 2.5\) bar/m.
So the profile is:
\[ p_A(z) = 0.6 + 2.5z \quad \text{(bar)} \]
Step 3: Determine the total pressure using the given boundary condition.
It is given that \(p_B \to 0\) at \(z = 0.8\) m. Since \(P = p_A+p_B\) is constant along the tube, at \(z=0.8\) m, \(P = p_A(0.8)\).
\[ p_A(0.8) = 0.6+2.5(0.8) = 0.6+2.0 = 2.6 \text{ bar} \]
So the (constant) total pressure is \(P = 2.6\) bar.
Step 4: Apply the condition \(p_A = p_B\) at \(z = z_1\).
Since \(p_A(z_1)+p_B(z_1)=P\) and \(p_A(z_1)=p_B(z_1)\):
\[ 2\,p_A(z_1) = P = 2.6 \ \Rightarrow \ p_A(z_1) = 1.3 \text{ bar} \]
Step 5: Solve for \(z_1\) using the linear profile from Step 2.
\[ 0.6 + 2.5 z_1 = 1.3 \]
\[ 2.5 z_1 = 0.7 \]
\[ z_1 = 0.28 \text{ m} \]
\[ \boxed{z_1 = 0.28 \text{ m}} \]