Abstract
The objective of this article is to model, by using a system of ordinary differential equations, the behavior of a reaction in a continuously stirred tank, a model that is highly presented in the industry in general and in particular in the pharmaceutical industry. Through the non-linear study of the response, pollutant concentration and temperature inside the reactor, we intend to determine the stable operating points for both the non-linear model and the linear model. The implementation of a proportional integral derivative controller will allow us to make the error signal null in a stable state in a closed loop with the respective gains for the proportional, integral, and derivative actions; said control is necessary and useful to be able to respond effectively and in a short time to the needs of the applications described, otherwise the dynamic system could not be used as a representation of the applied systems since time and control restrictions are strictly necessary. Keywords: Control, Nonlinear Dynamics, Steady State Error, Continuously Stirred Reactor, Controller Robustness DOI： https://doi.org/10.35741/issn.0258-2724.58.1.59
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