dc.contributor.author | Aguiar R.A. | |
dc.contributor.author | Franco I.C. | |
dc.contributor.author | Leonardi F. | |
dc.contributor.author | Lima F. | |
dc.date.accessioned | 2019-08-20T00:15:06Z | |
dc.date.accessioned | 2023-05-03T20:35:50Z | |
dc.date.available | 2019-08-20T00:15:06Z | |
dc.date.available | 2023-05-03T20:35:50Z | |
dc.date.issued | 2018 | |
dc.identifier.citation | AGUIAR, RENATO APARECIDO; FRANCO, Ivan Carlos; LEONARDI, Fabrizio; LIMA, FÁBIO. Fractional PID Controller Applied to a Chemical Plant with Level and pH Control. CHEMICAL PRODUCT AND PROCESS MODELING, v. 13, n. 4, p. 1-12, 2018. | |
dc.identifier.issn | 1934-2659 | |
dc.identifier.uri | https://hdl.handle.net/20.500.12032/89075 | |
dc.description.abstract | © 2018 Walter de Gruyter GmbH, Berlin/Boston.One of the most important processes in the chemical, biological and petrochemical industries is the control of the potential of hydrogen (pH). As it is a multivariable process and non-linear, pH control gives rise to many challenges for designers in both dynamic responses and robustness issues. Despite all this complexity, in many circumstances pH control is performed by using a conventional proportional integral derivative (PID) control, which is very common in industry. This paper proposes using a fractional-order PID to improve the pH control performance of a lab-scale process, as it is more flexible, i. e., there is a higher number of variables to be adjusted. Results from a simulation have been compared to those from both conventional and fractional-order PID controls, which has shown the better performance of the latter related to important metrics such as the control effort and dynamic response of the controlled variables. | |
dc.relation.ispartof | Chemical Product and Process Modeling | |
dc.rights | Acesso Restrito | |
dc.title | Fractional PID controller applied to a chemical plant with level and pH control | |
dc.type | Artigo | |