This paper is concerned with the robust stabilisation of a wide class of un
stable processes operated in continuous stirred tank reactors, For non-isot
hermal reactors, the regulated output is the temperature. For isothermal re
actors, the regulated output is the single concentration of either an initi
al reactant or a final product. In both cases the proposed control law is a
dynamic output feedback which can be interpreted as a straightforward modi
fication of a standard PI controller. In accordance with the engineering co
nstraints, the control action is positive and saturated With this control l
aw: it is shown that the output variable may be regulated at a prescribed s
et point despite a wide kinetic uncertainty. Furthermore, the controller ac
hieves a global stabilisation of the process in its domain of physical exis
tence. When the reactor is minimum phase, the closed loop has a single equi
librium which is globally asymptotically stable. When the reactor is non-mi
nimum phase phase, a global practical output regulation with state boundedn
ess is obtained with the same controller.