A control system based on a combination of the gain-scheduling control meth
od and an adaptive PID controller was designed for the production of xylose
from hardwood hemicellulose using a stirring tank reactor. Different opera
ting conditions have been considered for estimating the adjustable paramete
r (theta) to take into account the changes of energy of the system. The per
formance of the control system was studied first by numerical simulation, a
nd after implementation in the stirred tank reactor where the controller ac
tually works.