Temperature control of ethylene to butene-1 dimerization reactor

Industrial and Engineering Chemistry Research

Volumn 39, Issue 5, 2000, Pages 1320-1329

  Ali, Emad ^a   Al Humaizi, Khalid ^a  

^a KING SAUD UNIVERSITY   (Saudi Arabia)

Author keywords

[No Author keywords available]

Indexed keywords

BUTENES; ETHYLENE; LINEAR CONTROL SYSTEMS; MATHEMATICAL MODELS; PREDICTIVE CONTROL SYSTEMS; REACTION KINETICS; TEMPERATURE CONTROL; TWO TERM CONTROL SYSTEMS;

CONTINUOUSLY STIRRED TANK REACTORS; DIMERIZATION REACTIONS;

CHEMICAL REACTORS;

ETHYLENE;

ANALYTIC METHOD; ARTICLE; CATALYSIS; DIMERIZATION; REACTION ANALYSIS; REACTOR; RECYCLING; TASK PERFORMANCE; THERMOREGULATION;

EID: 0033627456     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie9903846     Document Type: Article

References (29)

1. Ali, E. Robust Model-Based Control of Open-loop Unstable Processes, the Arabian J. Sci. Eng. 1999, 24, 33-48.
2. Ali, E.; Abasaeed, A.; Al-zahrani, S. Optimization and Control of Industrial Gas-Phase Ethylene Polymerization Reactors. Ind. Eng. Chem. Res. 1998, 37, 3414-3423.
3. Astrom, K. J.; Hagglund, T. Automatic Tuning of Simple Regulators with Specifications of Phase and Amplitude Margins. Automatica 1984, 20 (5), 645-651.
4. Braunschweig, S.; Galtier, P.; Glaize, Y. ALEXIP. Revue De Einstitut Francais Du Petorle 1990, 47, 375-383.
5. Cao, Y.; Biss, D. An Extension of Singular Value Decomposition for Assessing Manipulated Variable Constraints. J. Proc. Cont. 1996, 6, 36.
6. Cao, Y.; Biss, D.; Perkins, J. Assessment of Input-Output Controllability in the Presence of Control Constraints. Comput. Chem. Eng. 1996, 20, 337-346.
7. Cohen, G. H.; Coon, G. A. Theoretical Investigations of Retarded Control. Trans. ASME 1953, 75, 827-834.
8. Cutler, C. R.; Ramaker, D. L. Dynamic Matrix Control-A Computer Control Algorithm. Proc. Joint Auto. Cont. Conf.; San Francisco, CA, 1980.
9. Dadebo, S.; Bell, M.; Mclellan, P.; McAuley, K. Temperature Control of Industrial Gas-Phase Polyethylene Reactors. J. Proc. Cont. 1997, 7, 83.
10. DePaor, A.; O'Malley, M. Controllers of Ziegler-Nichols Type for Unstable Process with Time Delay. Int. J. Control 1989, 49, 1273-1284.
11. Galtier, P. A.; Forestiere, A. A.; Glaize, Y. H.; Wauquire, J. P. Mathematical Modeling of Ethylene Oligomerization. Chem. Eng. Sci. 1988, 43, 1855-1860.
12. Lee, J. H.; Morari, M.; Garcia, E. State Space Interpretation of Model Predictive Control. Automatica 1994, 30, 707-717.
13. Luyben, W. Tuning Temperature Controllers on Open-loop Unstable Reactors. Ind. Eng. Chem. Res. 1998, 37, 4322-4331.
14. Ogunnaike, B. A. Dynamic Matrix Control: A Nonstochastic Industrial Process Control Technique with Parallel Applied Statistics. Ind. Eng. Chem. Fundam. 1986, 25, 712.
15. Poulin, E.; Pomerleau, A. PID Tuning for Integrating and Unstable Processes. IEE Proc. Cont. Theory. Appl. 1996, 143, 429-435.
16. Qin, J. S.; Badgwell, T. A. An Overview of Industrial Model Predictive Control Technology. Proc. Chem. Process Cont. Conf. CPC V; Kantor, J. C., Garcia, C. E., Carnahan, B., Eds.; AIChE Symp. Ser. 1997, 376 (93), 201.
17. Qin, J. S.; Badgwell, T. A. An Overview of Industrial Model Predictive Control Technology. Proc. Chem. Process Cont. Conf. CPC V; Kantor, J. C., Garcia, C. E., Carnahan, B., Eds.; AIChE Symp. Ser. 1997, 376 (93), 201.
18. Rawlings, J.; Muske, K. The Stability of Receding Horizon Control. IEEE Trans. Auto. Cont. 1993, 38, 1512-1516.
19. Rotstein, G.; Lewin, D. Simple PI and PID Tuning for Open-loop Unstable Systems. Ind. Eng. Chem. Res. 1991, 30, 1609-1615.
20. Seborg, D.; Edgar, T.; Mellichamp, D. Process Dynamics and Control; Wiley and Sons: New York, 1989.
21. Shridhar, R.; Cooper, D. J. A Tuning Strategy for Unconstrained SISO Model Predictive Control, Ind. Eng. Chem. Res. 1997, 36, 729-746.
22. Shridhar, R.; Cooper, D. J. A Tuning Strategy for Unconstrained Multivariable Model Predictive Control. Ind. Eng. Chem. Res. 1998, 37, 4003-4016.
23. Trabzoni, F. Modeling and Simulation of an Ethylene Dimerization Reactor Dynamics. M. Sc. Thesis, Chemical Engineering Department, King Saud University, Riyadh, Saudi Arabia, 1998.
24. Venkatashankar, V.; Chidambaram, M. Design of P and PI Controllers for Unstable First-Order Plus Time Delay Systems. Int. J. Control 1994, 60, 137-144.
25. Venkatashankar, V.; Chidambaram, M. On-line Controller Tuning for Unstable Systems. Comput. Chem. Eng. 1996, 20 (3), 301-305.
26. 3. J. Catal. 1991, 732, 68-78.
27. Yi, C.; Luyben, W. Evaluation of Plant-Wide Control Structures by Steady-State Disturbance Sensitivity Analysis. Ind. Eng. Chem. Res. 1995, 34, 2393-2405.
28. Yuwana, M.; Seborg, D. A New Method for On-line Controller Tuning. AIChE 1982, 28 (3), 434-439.
29. Ziegler, J.; Nichols, N. Optimum Settings for Automatic Controllers. Trans. ASME 1942, 64, 759-768.