Article ID Journal Published Year Pages File Type
153264 Chemical Engineering Journal 2008 9 Pages PDF
Abstract

Some chemical plants such as plug-flow tubular reactors have highly nonlinear behavior. Such processes demand a powerful identification method such as a neural-networks-based Wiener model. In this paper, a plug-flow reactor is simulated in a rather realistic environment by HYSYS, and the obtained data is in connection with MATLAB for identification and control purpose. The process is identified with NN-based Wiener identification method, and two linear and nonlinear model predictive controllers are applied with the ability of rejecting slowly varying unmeasured disturbances. The results are also compared with a common PI controller for temperature control of tubular reactor. Simulation results show that the obtained Wiener model has a good capability to predict the step response of the process. Parameters of both linear and nonlinear model predictive controllers are tuned and the best-obtained results are compared. For this purpose, different operating points are selected to have a wide range of operation for the nonlinear process. It is shown that the nonlinear controller has the fastest damped response in comparison with the other two controllers.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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