First Principle Modeling and Neural Network–Based Empirical Modeling with Experimental Validation of Binary Distillation Column
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Amit Kumar Singh
Amit Kumar Singh is currently working towards his Ph.D. degree in Department of Electrical Engineering at Indian Institute of Technology, Roorkee (India). His research interests include control system, process control and application of evolutionary techniques to chemical processes., Barjeev Tyagi
Barjeev Tyagi received B. Tech. degree in Electrical Engineering from University of Roorkee (India) in 1987 and Ph.D. degree from IIT Kanpur in 2006. Presently, he is Associate professor in Electrical Engineering Department at Indian Institute of Technology, Roorkee (India). His research interests include control system, power system deregulation, power system optimization and control.Vishal Kumar received the Ph.D. degree in power system engineering from the Indian Institute of Technology, Roorkee, India, in 2007. Currently, he is Assistant professor in the Department of Electrical Engineering, Indian Institute of Technology, Roorkee, India. His research interests include power distribution system operation and protection, and digital design and verification.
Abstract
To get the better product quality and to decrease the energy consumption of the distillation column, an accurate and suitable nonlinear model is crucial important. In this work, two types of model have been developed for an existing experimental setup of continuous binary distillation column (BDC). First model is a theoretical tray-to-tray binary distillation model for describing the steady-state behavior of composition in response to changes in reflux flows and in reboiler duty. Another model is an artificial neural network (ANN)–based input/output data relationship model. In ANN-based model, temperature of first tray, feed flow rate, and column pressures have been taken in addition to reflux flow rate and reboiler heat duty as inputs to give the more accurate I/O relationship. The comparison of output of ANN model and the equation-based model with the real-time output of the experimental setup of BDC has been given for the validation of developed models.
About the authors

Amit Kumar Singh is currently working towards his Ph.D. degree in Department of Electrical Engineering at Indian Institute of Technology, Roorkee (India). His research interests include control system, process control and application of evolutionary techniques to chemical processes.

Barjeev Tyagi received B. Tech. degree in Electrical Engineering from University of Roorkee (India) in 1987 and Ph.D. degree from IIT Kanpur in 2006. Presently, he is Associate professor in Electrical Engineering Department at Indian Institute of Technology, Roorkee (India). His research interests include control system, power system deregulation, power system optimization and control.

Vishal Kumar received the Ph.D. degree in power system engineering from the Indian Institute of Technology, Roorkee, India, in 2007. Currently, he is Assistant professor in the Department of Electrical Engineering, Indian Institute of Technology, Roorkee, India. His research interests include power distribution system operation and protection, and digital design and verification.
Acknowledgement
The authors wish to acknowledge the financial support of the Ministry of human resource and developments (MHRD), India under faculty initiation grant scheme with grant no. MHRD-03-29-801-108(FIG).
References
1. CanU, JimohM, SteinbachJ, WoznyG. Simulation and experimental analysis of operational failures in a distillation column. Separation Purif Technol2002;29:163–70.10.1016/S1383-5866(02)00072-2Search in Google Scholar
2. BansalV, PerkinsJD, PistikopoulosEN, RossR, van SchijndelJM, DesignS. Control optimization under uncertainty. Computers Chem Eng2000;24:261–6.10.1016/S0098-1354(00)00475-0Search in Google Scholar
3. DiehlM, FindeisenR, SchwarzkopfS, UsluI, AllgöwerF, BockHG, et al. An efficient algorithm for nonlinear model predictive control of large-scale systems part ii: experimental evaluation for a distillation column. Automatisierungstechnik2003;51:22–9.10.1524/auto.51.1.22.18879Search in Google Scholar
4. YangDR, LeeKS. Monitoring of a distillation column using modified extended Kalman filter and a reduced order model. Computers Chem Eng1997;21:565–70.10.1016/S0098-1354(97)87562-XSearch in Google Scholar
5. KumarA, DaoutidisP. Nonlinear model reduction and control of high-purity distillation columns. Proceeding of the American Control Conference, San Diego, CA, 1997.Search in Google Scholar
6. KienleA. Low-order dynamic models for ideal multicomponent distillation processes using nonlinear wave propagation theory. Chem Eng Sci2000;55:1817–28.10.1016/S0009-2509(99)00463-7Search in Google Scholar
7. HiglerA, ChandeR, TaylorR, BaurR, KrishnaR. Nonequilibrium modeling of three-phase distillation. Computers Chem Eng2004;28:2021–36.10.1016/j.compchemeng.2004.04.008Search in Google Scholar
8. BianS, HensonMA. Measurement selection for on-line estimation of nonlinear wave models for high purity distillation columns. Chem Eng Sci2006;61:3210–22.10.1016/j.ces.2005.11.066Search in Google Scholar
9. BarrosoJ, BorgesJ, OliveiraP, PinheiroCC, PiresAC, SilvaJM. Nonlinear modeling of a real pilot scale continuous distillation process. 20th European Symposium on Computer Aided Process Engineering– ESCAPE20.Search in Google Scholar
10. WenbinLi, BotanL, GuocongYu, XigangY. A numerical method for predicting the performance of a randomly packed distillation column. Int J Heat Mass Transfer2009;52:5330–8.10.1016/j.ijheatmasstransfer.2009.06.038Search in Google Scholar
11. MunteanI, StuckertM, AbrudeanM. A general distillation modeling framework applied to an isotopic distillation column. 19th Mediterranean Conference on Control and Automation Aquis Corfu Holiday Palace, Corfu, Greece, June 20–23, 2011.10.1109/MED.2011.5983157Search in Google Scholar
12. PearsonRK, PottmanM. Gray-box identification of block oriented nonlinear models. J Process Control2000;10:301–15.10.1016/S0959-1524(99)00055-4Search in Google Scholar
13. ZhuY. Distillation column identification for control using wiener model. Proceeding of the American Control Conference, San Diego, CA, 1999.Search in Google Scholar
14. BloemenHH, ChowCT, Van der BoomTT, VerdultV, VerhaegenM, BackxTC. Wiener model identification and predictive control for dual composition control of a distillation column. J Process Control2001;11:601–20.10.1016/S0959-1524(00)00056-1Search in Google Scholar
15. NugrohoS, NazaruddinYY, TjokronegoroHA. Non-linear identification of aqueous ammonia binary distillation column based on simple Hammerstein model. 5th Asian Control Conference, Melbourne, Australia, 2004.Search in Google Scholar
16. BrizuelaE, UriaM, LamannaR. Predictive control of a multi-component distillation column based on neural networks. Proceedings of the International Workshop on Neural Networks for Identification, Control, Robotics, and Signal/Image Processing (NICROSP ‘96), Venice, Italy, 1996.Search in Google Scholar
17. Savkovic–StevanovicJ. Neural net controller by inverse modeling for a distillation plant. Computers Chem Eng1996;20:925–30.10.1016/0098-1354(96)00162-7Search in Google Scholar
18. BarattiR, CortiS, ServidaA, Feedforward ControlA. Strategy for distillation columns. Artif Intelligence Eng1997;11:405–12.10.1016/S0954-1810(97)00002-2Search in Google Scholar
19. RamchandranS. Neural network control of distillation: an industrial application. Proceedings of the American Control Conference, Albuquerque, New Mexico, June 1997.10.1109/ACC.1997.611866Search in Google Scholar
20. YuX, NeuromorphicA. Controller for a distillation column. 4th IEEE International Conference on Control and Automation (ICCA), Montreal, QC, 2003.Search in Google Scholar
21. SinghAK, TyagiB, KumarV. Application of feed forward and recurrent neural network topologies for the modeling and identification of binary distillation column. IETE J Res2013;59:167–175.10.4103/0377-2063.113038Search in Google Scholar
22. SinghV, GuptaI, GuptaHO, BasedAN. Estimator for distillation-inferential control. Chem Eng Process2005;44:785–95.10.1016/j.cep.2004.08.010Search in Google Scholar
23. SinghV, GuptaI, GuptaHO, BasedANN-. Estimator for distillation using Levenberg–Marquardt approach. Eng Appl Artif Intelligence2007;20:249–59.10.1016/j.engappai.2006.06.017Search in Google Scholar
24. AbdullahZ, AhmadZ, AzizN. MIMO neural network model for pilot plant distillation column. 10th International Symposium on Process Systems Engineering (PSE2009).10.1016/S1570-7946(09)70309-8Search in Google Scholar
25. LiX, YuW. Modeling and neuro control for multicomponent nonideal distillation column. 2011 9th IEEE International Conference on Control and Automation (ICCA) Santiago, Chile, December 19–21, 2011.Search in Google Scholar
26. LuybenWL. Process modeling simulation and control for chemical engineers, 2nd ed. Auckland: McGraw-Hill, 1990.Search in Google Scholar
27. MarquardtDW. An algorithm for the least-squares estimation of nonlinear parameters. SIAM J Appl Math1963;11:431–41.10.1137/0111030Search in Google Scholar
28. LevenbergK. A method for the solution of certain non-linear problems in least squares. Q Appl Math1944;2:164–8.10.1090/qam/10666Search in Google Scholar
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