This article focuses on the design and implementation of model-based control strategies for
real time control of crystal size distribution (CSD) in semi batch crystallization processes …

In this work, a proportional/integral (PI) material-balance scheme to control continuous free-
radical solution homopolymer (possibly open-loop unstable) reactors with level …

Two-point and three-point temperature control structures are proposed for a kinetically
controlled ideal reactive distillation (RD) column. The control structures maintain stable …

The problem of reducing the energy consumption in an industrial multicomponent distillation
column is addressed. The column is subjected to step feed and distillate flow rates, the …

The problem of designing the state estimation structure for staged process is addressed
within a geometric estimation (GE) framework, with the class of binary columns as case …

Although the two-input− two-output (2I− 2O) dual composition (DC) and two-point
temperature (TPT) distillation control problems have been studied extensively, the …

In this study, we investigated the effects of partial condensation on the heat and mass
transfer rates during ethanol–water binary distillation based on a laminar boundary layer …

The two-point composition control problem of binary distillation columns is addressed. First,
the exact model-based inventory control problem is studied, yielding the underlying …

The milk pasteurization process is nonlinear in nature, and for this reason, the application of
linear control algorithms does not guarantee the obtainment of the required performance in …

Distillation columns have been widely used in chemical plants for separation process. The
high nonlinearity and dynamic behavior of the column make them hard to control. Internal …