This experimental work concerns the multivariable nonlinear control of a pilotsize
continuous polymerization reactor with generically singular characteristic matrix. The control …

This experimental work concerns the multivariable nonlinear control of a continuous stirred‐
tank polymerization reactor. The globally linearizing control (GLC) method is implemented to …

This work studies the experimental application of the globally linearizing control (GLC)
method to a batch polymerization reactor. The nonlinear controller is implemented on a …

In this experimental study, the Globally Linearizing Control (GLC) technique is applied to
control temperature and conversion in a continuous stirred tank polymerization reactor by …

A multivariable nonlinear control strategy which accounts for unmeasured state variables
and input constraints is developed for the free-radical polymerization of methyl methacrylate …

Continuous solution copolymerization is an important industrial process in the manufacture
of commodity and engineering plastics. The addition of comonomers and solvent, and the …

Presents an approach to the problem of nonlinear output feedback control. A nonlinear
output feedback control law is derived within the framework of input-output linearization. It …

This work concerns the synthesis of nonlinear controllers for multivariable nonlinear
processes that make the closed‐loop system linear in an input/output sense. Necessary and …

A multilayer control scheme is synthesized for a series of polymerization stirred tank reactors
to control the monomer conversion over the reactor line. In this work two layers of control are …

The problem of controlling (possibly open-loop unstable) continuous free-radical solution
polymer reactors with temperature, level and flow measurements is addressed. The …