Abstract
A novel double-loop control architecture with a fractional-order IMC (internal model control) in the outer loop is suggested for integrating plants with dead time and inverse response behavior. The inner loop controller is tuned using the maximum sensitivity concept to stabilize the plant, and it also enhances the disturbance response. The IMC controller is analytically designed to achieve improved closed-loop performance and robustness. The proposed tuning rules involve three design parameters \(\beta ,\alpha \) and \(\lambda \), whose method of selection is explained through extensive simulations and stability analysis. The suitability of the proposed control is verified for a wide class of processes, including higher-order and double-integrating processes with non-minimum phase characteristics. The suggested control has the capability of producing a fast and smooth set-point tracking response and rejecting the load disturbance effectively even in the presence of measurement noise. Random perturbations are also introduced in the process parameters to further investigate the system’s robustness.
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References
Luyben WL (2003) Identification and tuning of integrating processes with deadtime and inverse response. Ind Eng Chem Res 42(13):3030–3035
Seborg DE, Edgar TF, Mellichamp DA, Doyle FJ III (2016) Process dynamics and control. Wiley, Hoboken
Begum KG, Rao AS, Radhakrishnan T (2017) Enhanced IMC based PID controller design for non-minimum phase (NMP) integrating processes with time delays. ISA Trans 68:223–234
Chidambaram M, Sree RP (2003) A simple method of tuning PID controllers for integrator/dead-time processes. Comput Chem Eng 27(2):211–215
Kaya I, Tan N, Atherton DP (2006) A refinement procedure for PID controllers. Electr Eng 88:215–221
Skogestad S (2003) Simple analytic rules for model reduction and PID controller tuning. J Process Control 13(4):291–309. https://doi.org/10.1016/S0959-1524(02)00062-8
Chanti Babu D, Santosh Kumar DB, Padma Sree R (2016) Tuning of PID controllers for unstable systems using direct synthesis method. Indian Chem Eng 59(3):215–241. https://doi.org/10.1080/00194506.2016.1255570
Kumar S, Ajmeri M (2023) Enhanced design of PI controller with lead-lag filter for unstable and integrating plus time delay processes. Chem Prod Process Model 18(5):793–809. https://doi.org/10.1515/cppm-2023-0008
Rao AS, Rao V, Chidambaram M (2009) Direct synthesis-based controller design for integrating processes with time delay. J Frank Inst 346(1):38–56
Vanavil B, Krishna Chaitanya K, Seshagiri Rao A (2013) Improved PID controller design for unstable time delay processes based on direct synthesis method and maximum sensitivity. Int J Syst Sci 46(8):1349–1366. https://doi.org/10.1080/00207721.2013.822124
Panda RC (2009) Synthesis of PID controller for unstable and integrating processes. Chem Eng Sci 64(12):2807–2816
Gu D, Ou L, Wang P, Zhang W (2006) Relay feedback autotuning method for integrating processes with inverse response and time delay. Ind Eng Chem Res 45(9):3119–3132
Pai N-S, Chang S-C, Huang C-T (2010) Tuning PI/PID controllers for integrating processes with deadtime and inverse response by simple calculations. J Process Control 20(6):726–733
Ajmeri M, Ali A (2015) Two degree of freedom control scheme for unstable processes with small time delay. ISA Trans 56:308–326
Chandran K et al (2020) Modified cascade controller design for unstable processes with large dead time. IEEE Access 8:157022–157036
Jeng J-C, Lin S-W (2012) Robust proportional-integral-derivative controller design for stable/integrating processes with inverse response and time delay. Ind Eng Chem Res 51(6):2652–2665
Uma S, Chidambaram M, Rao AS (2010) Set point weighted modified Smith predictor with PID filter controllers for non-minimum-phase (NMP) integrating processes. Chem Eng Res Des 88(5–6):592–601
Nema S, Padhy PK (2015) Identification and cuckoo PI-PD controller design for stable and unstable processes. Trans Inst Meas Control 37(6):708–720. https://doi.org/10.1177/0142331214546351
Park JH, Sung SW, Lee I-B (1998) An enhanced PID control strategy for unstable processes. Automatica 34(6):751–756
Vijayan V, Panda RC (2012) Design of PID controllers in double feedback loops for SISO systems with set-point filters. ISA Trans 51(4):514–521
Kaya I (2020) Integral-proportional derivative tuning for optimal closed loop responses to control integrating processes with inverse response. Trans Inst Meas Control 42(16):3123–3134
Lloyds Raja G, Ali A (2021) New PI-PD controller design strategy for industrial unstable and integrating processes with dead time and inverse response. J Control Autom Electr Syst 32(2):266–280. https://doi.org/10.1007/s40313-020-00679-5
Kumari S, Aryan P, Raja GL (2021) Design and simulation of a novel FOIMC-PD/P double-loop control structure for CSTRs and bioreactors. Int J Chem React Eng 19(12):1287–1303
Mondal R, Dey J (2022) A novel design methodology on cascaded fractional order (FO) PI-PD control and its real time implementation to Cart-Inverted Pendulum System. ISA Trans 130:565–581
Gnaneshwar K, Trivedi R, Padhy PK (2022) Robust design of fractional order IMC controller for fractional order processes with time delay. Int J Numer Model Electron Netw Devices Fields 35(5):e3009
Ajmeri M, Ali A (2017) Analytical design of modified Smith predictor for unstable second-order processes with time delay. Int J Syst Sci 48(8):1671–1681
Begum KG, Rao AS, Radhakrishnan T (2016) Maximum sensitivity based analytical tuning rules for PID controllers for unstable dead time processes. Chem Eng Res Des 109:593–606
Skogestad S, Postlethwaite I (2005) Multivariable feedback control: analysis and design. Wiley, Hoboken
Ajmeri M (2024) Novel twofold control for delayed industrial processes with integrating and inverse response characteristics. IFAC J Syst Control 27:100242
Chen Y, Hu C, Moore KL (2003) Relay feedback tuning of robust PID controllers with iso-damping property. In: 42nd IEEE international conference on decision and control (IEEE Cat. No. 03CH37475) IEEE, Vol 3, pp 2180–2185
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Authors would like to thank NIT Patna and Darbhanga College of Engineering, Darbhanga, for providing opportunity to do research work.
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SK involved in contributions, conceptualization, simulations, theoretical development, result analysis and manuscript writing. MA involved in contributions, conceptualization, result analysis, manuscript writing and supervision.
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Kumar, S., Ajmeri, M. Analytically designed dual-loop fractional-order IMC for integrating plants with inverse behavior. Int. J. Dynam. Control (2024). https://doi.org/10.1007/s40435-024-01421-8
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DOI: https://doi.org/10.1007/s40435-024-01421-8