Evidence map›Paper›PMID 40348876›Full record

ArticleScientific reports2025

Quadratic interpolation optimization-based 2DoF-PID controller design for highly nonlinear continuous stirred-tank heater process.

Serdar Ekinci, Davut Izci, Veysel Gider, Mohit Bajaj, Vojtech Blazek, Lukas Prokop

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Article in Scientific reports, 2025. The graph could read no effect estimate from its abstract, so it casts no vote on the map. Cited by 6 papers.

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6citing papers in PubMed
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6 citing papers in PubMed.

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5 · Who and what money

Authors and funding

6 authors.

Serdar EkinciDepartment of Computer Engineering, Istanbul Gedik University, Istanbul, 34876, Turkey.
Davut IzciDepartment of Electrical and Electronics Engineering, Bursa Uludag University, Bursa, 16059, Turkey.
Veysel GiderDistance Education Application and Researcher Center, Batman University, Batman, Turkey.
Mohit BajajDepartment of Electrical Engineering, Graphic Era (Deemed to Be University), Dehradun, 248002, India. mohitbajaj.ee@geu.ac.in.
Vojtech BlazekENET Centre, CEET, VSB-Technical University of Ostrava, 708 00, Ostrava, Czech Republic.
Lukas ProkopENET Centre, CEET, VSB-Technical University of Ostrava, 708 00, Ostrava, Czech Republic.

Funding

European Union CZ.10.03.01/00/22_003/0000048ExPEDite (European Union's Horizon Mission Programme) 101139527National Centre for Energy II TN02000025
6 · The paper itself

Abstract

Temperature control in continuous stirred tank heater (CSTH) systems is essential for ensuring energy efficiency, safety, and product quality in industrial processes. However, the nonlinear dynamics and external disturbances make conventional proportional-integral-derivative (PID) control inadequate for reliable operation. This study presents a novel two-degrees-of-freedom PID (2DoF-PID) controller optimized using the quadratic interpolation optimization (QIO) algorithm to enhance CSTH temperature regulation. The QIO-based approach allows independent tuning for setpoint tracking and disturbance rejection, overcoming the limitations of classical PID controllers. Extensive nonlinear time-domain simulations, reference tracking, and disturbance rejection tests demonstrate the superior performance of the proposed controller in terms of reduced overshoot, faster settling time, and minimal steady-state error. Furthermore, comparative evaluations with traditional tuning methods (Murrill and Rovira) and several state-of-the-art metaheuristic optimizers (DE, PSO, FLA, MGO) validate the effectiveness and robustness of the QIO-optimized strategy. This work introduces a pioneering application of the QIO algorithm in industrial temperature control, offering a scalable and cost-efficient solution for complex nonlinear systems.

Indexed as

DegreesFreedom (2DoFOfPID) control scheme, continuous stirredQuadratic interpolation optimization, twoTank heater (CSTH), metaheuristic tuning methods, control of industrial processes

Identifiers

PMID40348876
PMCPMC12065853

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