Dynamic Control of Sensor and Actuator failures in Multivariable Distillation Column

Authors

  • Ali H. Al-Shatri Centre of Hydrogen Energy, Institute of Future Energy, Universiti Teknologi Malaysia
  • Arshad Ahmad Centre of Hydrogen Energy, Institute of Future Energy, Universiti Teknologi Malaysia
  • Olagoke Oladokun Centre of Hydrogen Energy, Institute of Future Energy, Universiti Teknologi Malaysia
  • Bemgba Bevan Nyakuma Centre of Hydrogen Energy, Institute of Future Energy, Universiti Teknologi Malaysia
  • Ali Al-shanini Department of Chemical Engineering, Hadhramout University, Mukalla

DOI:

https://doi.org/10.11113/jest.v2n2.12

Keywords:

Multivariable distillation column, abnormal process situations, PI-control, actuator failure, sensor failure

Abstract

This paper examines the impact of sensor and actuator failures in the operation of a multivariable distillation column. Several failure scenarios are evaluated including failures of sensors and actuators in various scales of magnitudes and durations. The results obtained illustrate the ability of process controllers in suppressing the impact of these unwanted events. Closed-loop dynamic responses of the process revealed capabilities of these controllers in dealing with upsets that are small in magnitude and duration. In the case of larger and longer process upsets, process controllers are not adequate in providing the necessary corrective measures. This leaves the necessary interventions to be taken by the plant operators, following alarms that would have been triggered in typical plant operation scenario.

References

Zumoffen, D., M. Basualdo. 2008. From Large Chemical Plant Data To Fault Diagnosis Integrated To Decentralized Fault-Tolerant Control: Pulp Mill Process Application. Industrial & Engineering Chemistry Research. 47(4): 1201-1220.

Rothenberg, D.H. 2009. Alarm Management for Process Control: A Best-practice Guide for Design, Implementation, and Use of Industrial Alarm Systems. Momentum Press.

Jelali, M. 2012. Control Performance Management In Industrial Automation: Assessment, Diagnosis And Improvement Of Control Loop Performance. Springer Science & Business Media.

Enagandula, S., J.B. Riggs. 2006. Distillation Control Configuration Selection Based On Product Variability Prediction. Control Engineering Practice. 14(7): 743-755.

Wahid, A., A. Ahmad. 2016. Improved Multi-Model Predictive Control To Reject Very Large Disturbances On A Distillation Column. International Journal of Technology. 6: 962-971.

Al-Shatri, A.H., A. Ahmad, N. Abdullah, O. Oladokun, A. Al-Shanini, M. Khalil. 2015. Control and Optimization Of Aromatic Compounds In Multivariable Distillation Column. Chemical Engineering Transactions. 45.

Marangoni, C., E. Zierhut, I. Parisotto, R. Machado, A. Bolzan. 2017. Influence of the Location of the Internal Temperature Control Loop on the Performance of the Dual Temperature Control for Feed Temperature Disturbance. Chemical and Biochemical Engineering Quarterly. 30(4): 411-418.

Kister, H.Z. 2003. What Caused Tower Malfunctions In The Last 50 Years? Chemical Engineering Research and Design. 81(1): 5-26.

Kanev, S.K. 2004. Robust Fault-Tolerant Control. University of Twente.

Isermann, R. 2005. Model-Based Fault-Detection And Diagnosis–Status And Applications. Annual Reviews in control. 29(1): 71-85.

Bullemer, P.T., L. Kiff, A. Tharanathan. 2011. Common Procedural Execution Failure Modes During Abnormal Situations. Journal Of Loss Prevention In The Process Industries. 24(6): 814-818.

Eljack, F., M.-K. Kazi. 2016. Process Safety And Abnormal Situation Management. Current Opinion In Chemical Engineering. 14: 35-41.

Al-Shatri, A.H., A. Ahmad, N. Abdullah, O. Oladokun, A. Al-shanini, M. Khalil. 2015. Control and Optimization of Aromatic Compounds in Multivariable Distillation Column. Chemical Engineering Transaction. 45: 469-474.

Skogestad, S. 1997. Dynamics and Control Of Distillation Columns: A Tutorial Introduction. Chemical Engineering Research and Design. 75(6): 539-562.

Halvorsen, I.J., S. Skogestad. 2003. Minimum Energy Consumption In Multicomponent Distillation. 3. More Than Three Products And Generalized Petlyuk Arrangements. Industrial & Engineering Chemistry Research. 42(3): 616-629.

Seborg, D.E., D.A. Mellichamp, T.F. Edgar, F.J. Doyle III. 2010. Process Dynamics And Control. John Wiley & Sons.

Åström, K.J., T. Hägglund. 2006. Advanced PID control. ISA-The Instrumentation, Systems and Automation Society.

Vu, T.N.L., M. Lee. 2010. Multi-loop PI Controller Design Based On The Direct Synthesis For Interacting Multi-Time Delay Processes. ISA transactions. 49(1): 79-86.

Ahmad, A., A. Samad, N.A. Fazli, A.W. Chow. 2003. Mathematical Modeling And Analysis Of Dynamic Behaviour Of A Fed-Batch Penicilin G Fermentation Process. Proceedings of International Conference on Chemical and Bioprocess Engineering. 387-394.

Marlin, T.E., T. Marlin. 1995. Process Control: Designing Processes And Control Systems For Dynamic Performance. McGraw-Hill New York.

Hurowitz, S., J. Anderson, M. Duvall, J.B. Riggs. 2003. Distillation Control Configuration Selection. Journal Of Process Control. 4(13): 357-362.

Ding, S.X. 2008. Model-Based Fault Diagnosis Techniques: Design Schemes, Algorithms, and Tools. Springer.

Yang, S.-F., H.-W. Ho, M.A. Rahim. 2007. Effects of Measurement Error On Controlling Two Dependent Process Steps. Economic Quality Control. 22(1): 127-139.

Bullemer, P.T., I. Nimmo. 1994. Understanding and supporting Abnormal Situation Management In Industrial Process Control Environments: A New Approach To Training. Systems, Man, and Cybernetics, 1994.'Humans, Information and Technology'., 1994 IEEE International Conference on. 391-396.

Monroy Chora, I. 2012. An Investigation On Automatic Systems For Fault Diagnosis In Chemical Processes.

Dash, S., V. Venkatasubramanian. 2003. Integrated framework For Abnormal Event Management And Process Hazards Analysis. AIChE Journal. 49(1): 124-139.

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Published

2019-12-09

How to Cite

Al-Shatri, A. H., Ahmad, A., Oladokun, O., Nyakuma, B. B., & Al-shanini, A. (2019). Dynamic Control of Sensor and Actuator failures in Multivariable Distillation Column. Journal of Energy and Safety Technology (JEST), 2(2). https://doi.org/10.11113/jest.v2n2.12

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Articles