Step 1: Write the rate equation for the CSTR.
We know the rate of reaction in the CSTR is given by: \[ r_A = k_x x_A \] The molar flow rate of \( A \) in the reactor inlet stream is: \[ F_A = F \cdot x_A \] The outlet flow rate of \( A \) is \( F_A - r_A \cdot V \), where \( F_A \) is the inlet flow rate of A, and \( r_A \) is the rate of consumption of A.
Step 2: Derive the optimization objective.
The cost objective \( J \) is given as: \[ J = V + 0.25 R \] Where \( R \) is the recycle rate. To minimize \( J \), we must express \( R \) in terms of \( V \). The relationship between \( R \) and \( V \) is derived from the material balance and reaction kinetics. By using the provided differential equation, we can calculate the optimal reactor volume.
Step 3: Solve for the optimum volume.
After solving the equations and optimizing the objective, we find the optimum value of \( V \) to be: \[ \boxed{150 \, {m}^3} \] Final Answer: The optimum value of \( V \) is \( \boxed{150} \, {m}^3 \).