“…In (A1) T, c : [0, 1] × R + → R with T(s, t) representing the reactor temperature at s ∈ [0, 1] and time t ≥ 0, c(s, t) the concentration, D being the diffusion coefficient, v the superficial velocity (assumed to be constant), η the heat interchange coefficient between the cooling jacket with temperature T c (s, t) (that can be used as a control input [27]), δ the adiabatic temperature rise, ρ : R + → R + the reaction rate function, γ the Arrhenius coefficient, and T e , c e the (constant) feed temperature and concentration, respectively.…”