Impact of industrial constraints on the dynamic performance of a PID-controlled hybrid heat-integrated distillation system with a plate heat and mass exchanger

• A PID-controlled HHIDiS system is dynamically modeled using Simulink/MATLAB. • Industrial constraints, including fouling and liquid hold up, affect thermal inertia and control. • Fouling and hold up of liquid alter dynamic responses and degrade PID control performance. • Periodic PID tuning mitigates adverse effects and ensures control quality under constraints. • HHIDiS remains dynamically stable, with PID controllers suitable for industrial applications. A dynamic model for the Hybrid Heat-Integrated Distillation System (HHIDiS) incorporating a Heat and Mass Exchanger (HME) was developed. The system’s behaviour under PID control was simulated using Simulink/MATLAB, with a focus on examining the effects of industrial constraints, such as fouling growth on heat exchanger surfaces and liquid hold up within the plate HME on operational quality indices. Results revealed that increases in fouling resistance or liquid hold up alter the thermal inertia of the HME, condenser, and reboiler, subsequently impacting the dynamic performance of PID control loops. These effects were analysed by simulating the closed-loop HHIDiS system at varying stages of fouling accumulation and liquid retention. Changes caused by fouling and liquid hold up were reflected in control quality indices such as overshoot, peak time, delay time, rise time, and settling time. Such variations may compromise PID control effectiveness. The findings emphasise the need to adjust PID tuning parameters to maintain optimal control performance when industrial constraints shift. Adverse effects can be mitigated through periodic recalibration of PID gains. Simulation results demonstrated that the proposed HHIDiS system remains dynamically stable despite these challenges and that standard PID controllers are suitable for its operation. These insights highlight the importance of proactive control adjustments to sustain high performance under evolving industrial conditions.

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Publication Details

Journal
International Journal of Heat and Mass Transfer
Published
2025-06-29
DOI
https://doi.org/10.1016/j.ijheatmasstransfer.2025.127445
Citations
3
Primary Topic
Process Optimization and Integration
Type
article
Field-Weighted Citation Impact
3.64
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article

Impact of industrial constraints on the dynamic performance of a PID-controlled hybrid heat-integrated distillation system with a plate heat and mass exchanger

Marian Trafczyński, Mariusz Markowski, Sławomir Alabrudziński, Krzysztof Urbaniec et al.
3 citations
International Journal of Heat and Mass Transfer
Process Optimization and Integration
3.64
article

Impact of industrial constraints on the dynamic performance of a PID-controlled hybrid heat-integrated distillation system with a plate heat and mass exchanger

Marian Trafczyński, Mariusz Markowski, Sławomir Alabrudziński, Krzysztof Urbaniec, P. Kisielewski, Erika Pavlovičová, Juraj Oravec, Kacper Elwertowski, Damian Gostynski
article en
3 citations

Abstract

• A PID-controlled HHIDiS system is dynamically modeled using Simulink/MATLAB. • Industrial constraints, including fouling and liquid hold up, affect thermal inertia and control. • Fouling and hold up of liquid alter dynamic responses and degrade PID control performance. • Periodic PID tuning mitigates adverse effects and ensures control quality under constraints. • HHIDiS remains dynamically stable, with PID controllers suitable for industrial applications. A dynamic model for the Hybrid Heat-Integrated Distillation System (HHIDiS) incorporating a Heat and Mass Exchanger (HME) was developed. The system’s behaviour under PID control was simulated using Simulink/MATLAB, with a focus on examining the effects of industrial constraints, such as fouling growth on heat exchanger surfaces and liquid hold up within the plate HME on operational quality indices. Results revealed that increases in fouling resistance or liquid hold up alter the thermal inertia of the HME, condenser, and reboiler, subsequently impacting the dynamic performance of PID control loops. These effects were analysed by simulating the closed-loop HHIDiS system at varying stages of fouling accumulation and liquid retention. Changes caused by fouling and liquid hold up were reflected in control quality indices such as overshoot, peak time, delay time, rise time, and settling time. Such variations may compromise PID control effectiveness. The findings emphasise the need to adjust PID tuning parameters to maintain optimal control performance when industrial constraints shift. Adverse effects can be mitigated through periodic recalibration of PID gains. Simulation results demonstrated that the proposed HHIDiS system remains dynamically stable despite these challenges and that standard PID controllers are suitable for its operation. These insights highlight the importance of proactive control adjustments to sustain high performance under evolving industrial conditions.

International Journal of Heat and Mass TransferVol. 252
Warsaw University of Technology (PL), Slovak University of Technology in Bratislava (SK)
Affordable and clean energy
Openalex Percentile: Top 7%
Process Optimization and Integration
3.64
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