Design and Control of Nonlinear Hybrid Tank Process using Conventional Controllers in Petrochemical Industries
Vinothkumar. C1, Marshiana. D2, Ramadevi. R3, Krishnamoorthy. N. R4

1Vinothkumar.C*, Department of EIE, Sathyabama Institute of Science and Technology, Chennai, India.
2Marshiana.D, Department of EIE, Sathyabama Institute of Science and Technology, Chennai, India.
3Ramadevi.R,  Department of EIE, Sathyabama Institute of Science and Technology, Chennai, India.
4Krishnamoorthy. N.R, Department of EIE, Sathyabama Institute of Science and Technology, Chennai, India.
Manuscript received on September 12, 2019. | Revised Manuscript received on October 20, 2019. | Manuscript published on October 30, 2019. | PP: 74-77 | Volume-9 Issue-1, October 2019 | Retrieval Number: A1048109119/2019©BEIESP | DOI: 10.35940/ijeat.A1048.109119
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Abstract: In this paper the plan of customary controllers, which can be utilized for the control of non-straight frameworks to give an ideal degree of a nonlinear tank. The non linear process takes up for the examination is Hybrid tanks due to its utilization in the field of Pharmaceutical, petro chemical ect., Its non-linearity is because of the cross sectional conduct of the procedure because of the departure of items without wastage is conceivable. The shut circle execution are resolved to get the ideal level control utilizing customary P , PI, PID controllers for different systems like Ziegler Nicholas and Cohen coon technique. The real preferred position of this strategy is straightforwardness. Reproduction results utilizing MATLAB programming to decide the outperformance of controller strategies.
Keywords: Hybrid Tank, Level Control, P, PI and PID controller, Petrochemical Industries, MATLAB software.