Abstract :
This paper describes a gray-box identi®cation approach to three classes of block-oriented models: Hammerstein models, Wiener
models, and the feedback block-oriented models introduced recently for modeling processes with output multiplicities. Here, we
restrict consideration to processes with nonlinear steady-state characteristics that are known a priori and do not exhibit steady-state
multiplicities. Under this assumption, simple identi®cation procedures may be developed for all three of these model structures, which
may be viewed as three dierent ways of combining a single static nonlinearity with a linear dynamic model with speci®ed steady-state
gain constraints. In particular, if the steady-state gain of the linear dynamic model is constrained to be 1, the steady-state character-
istic of the overall model is determined entirely by the static nonlinearity. If the steady-state characteristic of the process is known, the
nonlinear component of the model may be determined from this knowledge, and the parameters of the linear model may be estimated
from input-output data. Detailed descriptions of simple least squares solutions of this identi®cation problem are presented, and the
approach is illustrated for a simple ®rst-principles model of a distillation column.
Keywords :
Wiener models , Steady-statemultiplicity , Chemical process modelling and control , Nonlinear system identi®cation , Model structure selection , Hammerstein models