Dual-loop PID control strategy for ramp tracking and ramp disturbance handling for unstable CSTRs

Abstract Control strategies designed for step signals fail when applied for ramp tracking and ramp disturbance rejection. Hence, this work presents a novel dual-loop control technique for ramp tracking and ramp disturbance rejection in unstable systems. To begin with, first the unstable process is stabilized using a proportional-derivative (PD) compensator (in the internal loop). This PD compensator was created utilising the direct synthesis approach. Using the loop shaping approach, a proportional-integral-derivative controller (in the outer-loop) is then developed to integrate stabilised plant dynamics. Simulations are done using standard unstable CSTR (Continuous Stirred Tank Reactor) plant models by applying step/ramp reference signals and disturbances. The proposed control strategy shows a satisfactory servo and regulatory response than the existing designs while dealing with step and ramp types of signals. Lastly, a performance summary is also presented on different errors.

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Publication Details

Journal
Chemical Product and Process Modeling
Published
2024-12-01
DOI
https://doi.org/10.1515/cppm-2024-0081
Citations
11
Primary Topic
Advanced Control Systems Design
Type
article
Field-Weighted Citation Impact
3.61
Controls
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article

Dual-loop PID control strategy for ramp tracking and ramp disturbance handling for unstable CSTRs

Dipjyoti Das, Deepak Kumar, G. Lloyds Raja, Sudipta Chakraborty
11 citations
Chemical Product and Process Modeling
Advanced Control Systems Design
3.61
article

Dual-loop PID control strategy for ramp tracking and ramp disturbance handling for unstable CSTRs

Dipjyoti Das, Deepak Kumar, G. Lloyds Raja, Sudipta Chakraborty
article en
11 citations

Abstract

Abstract Control strategies designed for step signals fail when applied for ramp tracking and ramp disturbance rejection. Hence, this work presents a novel dual-loop control technique for ramp tracking and ramp disturbance rejection in unstable systems. To begin with, first the unstable process is stabilized using a proportional-derivative (PD) compensator (in the internal loop). This PD compensator was created utilising the direct synthesis approach. Using the loop shaping approach, a proportional-integral-derivative controller (in the outer-loop) is then developed to integrate stabilised plant dynamics. Simulations are done using standard unstable CSTR (Continuous Stirred Tank Reactor) plant models by applying step/ramp reference signals and disturbances. The proposed control strategy shows a satisfactory servo and regulatory response than the existing designs while dealing with step and ramp types of signals. Lastly, a performance summary is also presented on different errors.

Chemical Product and Process ModelingVol. 19(6)
National Institute of Technology Patna (IN), National Institute Of Technology Silchar (IN)
Openalex Percentile: Top 6%
Advanced Control Systems Design
3.61
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