A generalized nonlinear mathematical model for fixed-bed tubular chemi
cal reactors with cooling is proposed. The model is suitable for simul
ation experiments. A strategy, focused on simplifying and adapting the
''primary'' model to control applications is shown. This procedure is
driven through the so-called ''pseudohomogeneous'' form of the model
until a final description which is linear and relatively simple. The r
esulting model is offered as a good basis for optimal control design.
Some simulation events are included.