Blending is an important unit operation in chemical process industries
. Based on Luyben's work, a coordinated control is proposed to overcom
e the system interaction and process nonlinearity in blending processe
s. Blending systems with ideal and nonideal mixing (by nonideal mixing
we mean the blended property is not a linear function of the inlet pr
operties) are explored. Furthermore, unusual dynamic behavior is obser
ved for blending systems coupled with complex dynamics arisen from the
process side. Controlling the blending of streams from different side
stream locations of a distillation column is studied and, based on phy
sical insight, a simple procedure is proposed for the selection of sid
edraw locations. Since, the properties of the inlet streams are often
subject to changes and disturbance rejection aspects of blending contr
ol are discussed and practically important issues such as model uncert
ainties and measurement noise are also treated in a rigorous manner. S
imulation results show that the control of blending systems is not as
trivial as it was thought and, more importantly, improvement in the pe
rformance can be achieved using the proposed coordinated control.