Fractional-order model identification based on the process reaction curve: a unified framework for chemical processes
dc.contributor.author | Gude, Juan José | |
dc.contributor.author | García Bringas, Pablo | |
dc.contributor.author | Herrera, Marco | |
dc.contributor.author | Rincón, Luis | |
dc.contributor.author | Teodoro, Antonio di | |
dc.contributor.author | Camacho, Oscar | |
dc.date.accessioned | 2024-11-15T10:09:33Z | |
dc.date.available | 2024-11-15T10:09:33Z | |
dc.date.issued | 2024-03 | |
dc.date.updated | 2024-11-15T10:09:33Z | |
dc.description.abstract | This study introduces a novel method for identifying dynamic systems aimed at deriving reduced-fractional-order models. Applicable to processes exhibiting an S-shaped step response, the method effectively characterizes fractional behavior within the range of fractional orders (α∈[0.5,1.0]). The uniqueness of this approach lies in its hybrid nature, combining one-variable optimization techniques for estimating the model fractional order α with analytical expressions to estimate parameters T and L. This hybrid approach leverages information from the reaction curve obtained through an open-loop step-test experiment. The proposed method demonstrates its efficacy and simplicity through several illustrative examples, showcasing its advantages over established analytical and optimization-based techniques. Notably, the hybrid approach proves particularly advantageous compared to methods relying on the process reaction curve. To highlight its practical applicability, the identification algorithm based on this hybrid approach is implemented on hardware using a microprocessor. The experimental prototype successfully identifies the First-Order Plus Dead Time (FFOPDT) model of a thermal-based process, validating the proposed method's real-world utility. | en |
dc.description.sponsorship | A. Di Teodoro and O. Camacho thank the Universidad San Francisco de Quito for supporting this work through the Poli-Grants Program under Grant 17965. Juan J. Gude and Pablo García Bringas thank the Basque Government for its funding support through the BEREZ-IA Elkartek project (ref. KK-2023/00012) | en |
dc.identifier.citation | Gude, J. J., García Bringas, P., Herrera, M., Rincón, L., Di Teodoro, A., & Camacho, O. (2024). Fractional-order model identification based on the process reaction curve: A unified framework for chemical processes. Results in Engineering, 21. https://doi.org/10.1016/J.RINENG.2024.101757 | |
dc.identifier.doi | 10.1016/J.RINENG.2024.101757 | |
dc.identifier.issn | 2590-1230 | |
dc.identifier.uri | http://hdl.handle.net/20.500.14454/1898 | |
dc.language.iso | eng | |
dc.publisher | Elsevier B.V. | |
dc.rights | © 2024 The Author(s) | |
dc.subject.other | Fractional first-order plus dead-time model | |
dc.subject.other | Fractional-order systems | |
dc.subject.other | Optimization | |
dc.subject.other | Process identification | |
dc.title | Fractional-order model identification based on the process reaction curve: a unified framework for chemical processes | en |
dc.type | journal article | |
dcterms.accessRights | open access | |
oaire.citation.title | Results in Engineering | |
oaire.citation.volume | 21 | |
oaire.licenseCondition | https://creativecommons.org/licenses/by-nc-nd/4.0/ | |
oaire.version | VoR |
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