ANALYSIS OF MULTIVARIABLE CONTROLLER FOR FLUID CATALYTIC CRACKING UNIT IN A PETROLEUM REFINERY

Authors

  • Elamurugan P Chettinad College of Engineering and Technology Puliyur, Karur 639 114, India
  • Siva K Hindusthan College of Engineering and Technology, Coimbatore, India

DOI:

https://doi.org/10.24297/jac.v12i18.605

Keywords:

FCCU, Control, PID, IMC, MPC

Abstract

The projected paper has been scrutinized and revised the circulated experimental results related to reactor-regenerator structure of fluid catalytic cracking unit (FCCU). It correspondingly focuses the limitations of existing methods for controlling the heat in the reactor-regenerator system. Now the extant study, complex dynamic model of the reactor–regenerator system has been industrialized and successively castoff with the controller. FCC process is considered as a primary conversion unit in a incorporated refinery and epitome FCC operation can have a significant impact on the refinery profitability. Control of the FCC continues to be a stimulating and momentous problem due to interaction between the loops. So there is a tangible requisite for a control logic that effectively utilizes the available process measurements and archetypal information representative of the process. Internal Model Controller (IMC) discloses the set point tracking Stabilization can be succeeded through simulated implementation of a model predictive control (MPC).

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Author Biographies

Elamurugan P, Chettinad College of Engineering and Technology Puliyur, Karur 639 114, India

Department of Electrical and Electronics Engineering,

Siva K, Hindusthan College of Engineering and Technology, Coimbatore, India

Department of Mechanical Engineering,

References

1. Elamurugan, P. and Dinesh Kumar, D. 2010 Modeling and Control of Fluid Catalytic Cracking Unit in Petroleum Refinery. International Journal of Computer Communication and Information System.,2(1), 55-59.
2. Jafar Sadeghzadeh Ahari., Amir Farshi, and Khaled Forsat. 2008 A Mathematical modeling of riser reactor in industrial unit. Petroleum & coal, 50(2), 15-24.
3. Rajeev, N., Krishna Prasad, and Reddy Ragul,U.B. 2015 Process Simulation and Modeling of Fluidized Catalytic Cracker Performance in Crude Refinery.Petroleum Science and Technology. 33(2015),110–117.
4. Diwakar T. Korsane, Vivek Yadav, and Kiran Raut, H. 2014 PID Tuning Rules for First Order plus Time Delay System. International journal of innovative research in electrical, electronics, instrumentation and control engineering.2(1),582-586.
5. Ramneet Singh, Rajni Bala, and Bhavi Bhatia, Internal Model Control (IMC) and IMC Based PID Controller, International Journal of Advanced Research in Computer Science and Software Engineering, 4(6), 2014, 915-922
6. Sivakumar, R. and Shennes Mathew, 2013 Design and Development of Model Predictive Controller for Binary Distillation Column. International Journal of Science and Research, 2(12), 445-451.
7. Chunyang Jia, Soharb Rohani, and Arthur Jutan, 2003 FCC unit modeling, identification and model predictive control, a simulation study. Chemical Engineering and processing, 42,(2003), 311-325.

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Published

2016-09-16

How to Cite

P, E., & K, S. (2016). ANALYSIS OF MULTIVARIABLE CONTROLLER FOR FLUID CATALYTIC CRACKING UNIT IN A PETROLEUM REFINERY. JOURNAL OF ADVANCES IN CHEMISTRY, 12(18), 5088–5095. https://doi.org/10.24297/jac.v12i18.605

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Articles