Jf. Forbes et Te. Marlin, MODEL ACCURACY FOR ECONOMIC OPTIMIZING CONTROLLERS - THE BIAS UPDATE CASE, Industrial & engineering chemistry research, 33(8), 1994, pp. 1919-1929
In many advanced control applications the numbers of manipulated and c
ontrolled variables are not the same. A combination of steady-state ec
onomic optimization and model predictive control has been employed to
exploit the optimization opportunities presented by such ''non-square'
' systems. The economic optimization subsystem uses a process model an
d is usually coupled with a model updating scheme to compensate for pl
ant/model mismatch. Care must be exercised during the design of such a
system to ensure the model-based optimization yields operating condit
ions which are optimal for the true plant. This paper presents a rigor
ous criterion for determining under what conditions the model-based op
timization embedded within the model predictive controller, using bias
update, is capable of finding the plant optimum despite plant/model m
ismatch. The model accuracy criterion can be applied by solving an app
ropriate nonlinear programming problem. Further, it is shown that when
the embedded model-based optimization problem has linear constraints,
the bias update method will ensure convergence to the plant optimum,
providing the model accuracy criterion is satisfied and an appropriate
filter is included in the feedback path. Discussions are concluded wi
th a demonstration of the methods on a real-time gasoline blending con
trol and optimization problem.