Multi loop Controller Design for Multivariable Processes Employing SISO PI Tuning Rules
G. Vamsi Krishna1, Naregalkar Akshay2
1G. Vamsi Krishna, Department of Electronics and Instrumentation Engineering, Vallurupalli Nageswara Rao Vignana Jyothi Institute of Engineering & Technology, Hyderabad, Telangana, India.
2Naregalkar Akshay, Department of Electronics and Instrumentation Engineering, Vallurupalli Nageswara Rao Vignana Jyothi Institute of Engineering & Technology, Hyderabad, Telangana, India.
Manuscript received on 08 April 2019 | Revised Manuscript received on 15 April 2019 | Manuscript Published on 26 July 2019 | PP: 347-351 | Volume-8 Issue-6S4 April 2019 | Retrieval Number: F10700486S419/19©BEIESP | DOI: 10.35940/ijitee.F1070.0486S419
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© The Authors. Blue Eyes Intelligence Engineering and Sciences Publication (BEIESP). This is an open-access article under the CC-BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/)
Abstract: Ability of the proportional integral (PI) and proportional integral derivative (PID) controllers in set point tracking and disturbance rejection has led to their wide usage in industrial applications. The desired controller performance can be achieved by application of suitable tuning rules. The presence of interacting loops in a process makes it a challenging task of PI controllers design in multivariable processes. This problem highly mitigated by employing simple single input single output internal model controller (IMC). This IMC PI controller values are applied for different distillation process involving distillation columns like Wardle and Wood (WW) , Wood and Berry (WB) and Vinate-Luyben (V-L). The obtained simulation with proposed method gives better results and performance indices values compared to other control tuning strategies.
Keywords: PI Controller; Tuning Mulivariable Process IMC SIMC BLT.
Scope of the Article: Process & Device Technologies