Model of idealized stirred tank reactor from [1], p. 280. In the stirred tank there is a continuous intake of substance A which reacts with a catalyzer and brakes down into other substances. Since the content of the tank reactor is stired continuously, it can be supposed a homogeneous distribution of all substances within the tank. Therefore, the tank reactor system can be described by means of concentrated parameters.
The chemical reaction in the tank reactor is exothermic, i.e. it
produces themal energy which affects the stability of the reaction.
To stabilize it, the tank reactor is cooled. The
temperature T_c of cooling medium is the variable
to be actuated by controller.
The speed γ of the reaction depends on the
concentration c and
temperature T as follows:
gamma = (1-x1) * k0 * e^(-eps/(1+x2))
with related concentration x1 and related
temperature x2:
c0 - c T - T0
x1 = --------; x2 = --------.
c0 T0
Both variables x1 and x2 are
states of the model. Additionally, there is used related
temperature u of cooling medium:
T_c - T0
u = --------.
T0