pH control is recognized as an industrially important, yet notoriously diff
icult control problem, Wiener models, consisting of a linear dynamic elemen
t followed in series by a static nonlinear element, are considered to be id
eal for representing this and several other nonlinear processes. Wiener mod
els require little more effort in development than a standard Linear step-r
esponse model, yet offer superior characterization of systems with highly n
onlinear gains. These models may be incorporated into model predictive cont
rol (MPC) schemes in a unique way which effectively removes the nonlinearit
y from the control problem, preserving many of the favorable properties of
linear MPC. In this paper, Wiener model predictive control (WMPC) is evalua
ted experimentally, and also compared with benchmark proportional integral
derivative (PID) and linear MPC strategies, considering the effects of outp
ut constraints and modeling error.