Chapter 1, Problem 1.8P

What is wrong with this solution? The irreversible liquid phase second order reaction ( $-r_{\text{A}}=k{C}_{\text{A}}^2$)

$\text{2A}\stackrel{k_1}{\to }\text{B}k=0.03{\text{dm}}^3\text{/mol}\cdot \text{s}$

is carried out in a CSTR. The entering concentration of A, C_A0, is 2 molar. and the exit concentration of A, C_A is 0.1 molar. The volumetric flow rate, v₀, is constant at 3 dm³/s. What is the corresponding reactor volume?