A CSTR has one feed stream F1, and one exit stream, F2. The feed contains pure species A, which undergoes a second order reaction in side the reactor. The term for the exit stream to the reactor in the differential equation that describes the change in concentration of A, $\frac{dC_A}{dt}$, is best represented by:
$-C_A^2 k_0 e^{\frac{-E_a}{RT}}$
$F_2C_{A,2}$
$C_A^2 k_0 e^{\frac{-E_a}{RT}}$
$F_1C_{A,1}$
$-F_2C_{A,2}$
$-F_1C_{A,1}$