Chemical Reactor Design and Control

Chemical Reactor Design and Control

Volumn , Issue , 2006, Pages 1-419

  Luyben, William L ^a  

^a LEHIGH UNIVERSITY   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

BATCH REACTORS; COMPUTER SOFTWARE; STRUCTURAL DESIGN;

CONTINUOUS STIRRED TANKS; CONTROL PROBLEMS; DYNAMIC CONTROLS; INDUSTRIAL REACTORS; PRACTICAL CONTROLS; PROCESS SIMULATORS; SIMULTANEOUS DESIGN AND CONTROL; STEADY-STATE DESIGN;

PROCESS CONTROL;

EID: 84947566756     PISSN: None     EISSN: None     Source Type: Book    
DOI: 10.1002/9780470134917     Document Type: Book

References (35)

1. C. J. Geankoplis, Transport Processes and Unit Operations, 3rd edition, Prentice-Hall, 1993, pp. 238, 300, 302.
2. W. Himmelsbach, D. Houlton, D. Ortlieb, and M. Lovallo. New advances in agitation technology for exothermic reactions in very large reactors, Chem. Eng. Sci. 61, 3044-3052 (2006).
3. F. G. Shinskey, Process Control Systems, 3rd edition, McGraw-Hill, 1988, p. 390.
4. A. Dourado, G. Goma, U. Albuquerque, and Y. Sevely, Modeling and the static optimization of the ethanol production in a cascade reactor-1. Modeling, Biotechnol. Bioeng., 29, 187-194 (1987).
5. G. R. Cysewski and C. R. Wilke, Process design and economic studies of alternative fermentation methods for the production of ethanol, Biotechnol. Bioeng., 20, 1421-1444 (1978).
6. J. Nielsen, J. Villadsen, and G. Lindén, Bioreaction Engineering Principles, 2nd ed., Springer, 2005.
7. B. W. Bequette, Process Dynamics: Modeling, Analysis and Simulation, Module 8, Prentice-Hall, 1998, p. 529.
8. A. Marchetti, M. Amrhein, B. Chachuat, and D. Bonvin, Scale-up of batch processes via decentralized control, ADCHEM IFAC, 2006, p. 221.
9. R. Smith and L. Choong, Optimizing batch operations, Chem. Eng. Prog., 102, 31-36 (Jan. 2006).
10. P. Jaisathaporn and W. L. Luyben, Ind. Eng. Chem. Res., 42, 3304. (2003).
11. W. E. Schiesser, The Numerical Method of Lines, Academic Press, 1991.
12. R. Shinnar, F. J. Doyle, H. M. Budman, and M. Morari. Design considerations for tubular reactors with highly exothermic reactions, AICHE J., 38, 1729 (1992).
13. 3 catalyst, J. Catalysis, 161, 1-10 (1996).
14. W. L. Luyben, Effect of kinetic, design and operating parameters on reactor gain, Ind. Eng. Chem. Research 39, 2384 (2000).
15. W. L. Luyben, Design and control of gas-phase reactor/recycle processes with reversible exothermic reactions, Ind. Eng. Chem. Research 39, 1529 (2000).
16. T. R. Elliott, M. L. Luyben, and W. L. Luyben, Application of the capacity-based economic approach to an industrial-scale process, Ind. Eng Chem. Research 36, 1727 (1997).
17. L. L. Upson, F. S. Rosser, C. L. Helmer, P. Palmas, L. E. Bell, W. J. Reagan, and B. W. Hedrick, Fluid catalytic cracking (FCC) units, Regeneration, Kirk-Othmer Encyclopedia of Chemical Technology, 5th Ed., Vol. 11, John Wiley & Sons, 2001.
18. R. Shinnar, A. Arbel, and I. H. Rinard, Dynamics and control of fluidized catalytic crackers. 3. Designing the control system: Choice of manipulated and measured variables for partial control, Ind. Eng. Chem. Res., 35(7), 2215-2233 (1996).
19. Ö. Uygun, H. Taşkin, C. Kubat, and S. Arslankaya, FUZZYFCC: Fuzzy logic control of a fluid catalytic cracking unit (FCCU) to improve dynamic performance, Computers & Chemical Engineering, 30(5), 850-863 (2006).
20. C. Higman and M. van der Burgt, Gasification, Elsevier, 2003.
21. L. J. Shadle, D. A. Berry, and M. Syamlal, Coal conversion processes, gasification, Kirk-Othmer Encyclopedia of Chemical Technology, 5th Ed., John Wiley & Sons, 2001.
22. G. Xu, T. Murakami, T. Suda, Y. Matsuzawa, and H. Tani, The superior technical choice for dual fludized bed gasification, Ind. Eng. Chem. Research, 45, 2281-2286 (2003).
23. R. Dixon, Advanced gasifier control, Comput. Control. Eng. J. IEE, 10(3), 93-96 (1999).
24. R. K. Al Seyab and Y. Cao, Nonlinear model predictive control of the ALSTOM gasifier, J. Process Control, 16, 795-808 (2006).
25. P. A. Wisnewski and F. J. Doyle, Control structure selection and model predictive control of the Weyerhaeuser digester problem, J. Process Control, 8, 487-495 (1998).
26. F. J. Doyle and F. Kayihan, Reaction profile control of the continuous pulp digester, Chem. Eng. Sci., 54, 2679-2688 (1999).
27. F. Kayihan, M. S. Gelormina, E. M. Hanczyc, F. J. Doyle, and Y. A. Arkun, A Kamyr continuous digester model for identification and controller design, Proc. IFAC World Congress, San Francisco, CA 1996, pp. 37-42.
28. J. R. Richards and J. P. Congalidis, Measurement and control of polymerization reactors, Comput. Chem. Eng., 30, 1447-1463 (2006).
29. W. H. Ray, Polymerization reactor control, IEEE Control Sys. Mag., 3-8 (Aug. 1986).
30. M. Asteausuain, A. Bandoni, C. Sarmoria, and A. Brandolin, Simultaneous process and control system design for grade transition in styrene polymerization, Chem. Eng. Sci., 61, 3362-3378 (2006).
31. J. S. Alford, Biprocess control: Advances and challenges, Comput. Chem. Eng., 30, 1464-1475 (2006).
32. W. Bequette, Process Control: Modeling, Design, and Simulation, Prentice-Hall, 2003.
33. A. Cinar, S. J. Parulekar, C. Undey, and G. Birol, Batch Fermentation: Modeling, Monitoring, and Control, Marcel Dekker, 2003.
34. S. De Wolf, R. L. E. Cuypers, L. C. Zullo, B. J. Vos, and B. J. Bax, Model predictive control of a slurry polymerization reactor, Comput. Chem. Eng., 20(Suppl.), S955-S961 (1996).
35. M. V. Kothare, Dynamics and control of integrated microchemical systems with application to micro-scale fuel processing, Comput. Chem. Eng., 30, 1725-1734 (2006).