Control of systems integrating logic, dynamics, and constraints
Automatica (Journal of IFAC)
Hi-index | 0.00 |
Almost all chemical processes are inherently nonlinear, whereas not all of them require nonlinear control. This leads to an interesting question "when is a linear controller adequate and when is a nonlinear controller warranted?" This paper proposes a nonlinearity measure based on gap metric to quantify the nonlinearity degree of chemical processes, aiming to answer such a question. The proposed measure is of great use to analysis and synthesis of nonlinear systems. A benchmark continuous stirred tank reactor (CSTR) process and a double effect evaporator (DEE) system are presented to illustrate the effectiveness to the proposed nonlinearity measure.