Buffer tank design for acceptable control performance

Industrial and Engineering Chemistry Research

Volumn 42, Issue 10, 2003, Pages 2198-2208

  Faanes, Audun ^a,b   Skogestad, Sigurd ^a  

^a NORWEGIAN UNIVERSITY OF SCIENCE AND TECHNOLOGY   (Norway)

^b STATOIL   (Norway)

Author keywords

[No Author keywords available]

Indexed keywords

FEEDBACK CONTROL; MIXING; TANKS (CONTAINERS);

BUFFER TANKS;

CHEMICAL ENGINEERING;

BUFFER;

DESIGN;

ARTICLE; BUFFER TANK; CALCULATION; CHEMICAL ENGINEERING; FEEDBACK SYSTEM; FLOW KINETICS; FLOW RATE; PROCESS DESIGN; QUALITY CONTROL; STEADY STATE; TANK; TEMPERATURE; TRANSPORT KINETICS;

EID: 0038665556     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie020525v     Document Type: Article

References (23)

1. Lieberman, N. P. Process Design for Reliable Operations; Gulf Publishing Co.: Houston, TX, 1983.
2. Sandler, H. J.; Luckiewicz, E. T. Practical Process Engineering; McGraw-Hill Book Co.: New York, 1987.
3. Ulrich, G. D. A Guide to Chemical Engingeering Process Design and Economics; John Wiley & Sons: New York, 1984.
4. Walas, S. M. Rules of thumb, selecting and designing equipment. Chem. Eng. 1987, 94 (4), 75-81.
5. Wells, G. L. The Art of Chemical Process Design; Elsevier: Amsterdam, The Netherlands, 1986.
6. Sigales, B, How to design reflux drums. Chem. Eng. 1975, 82 (5), 157-160.
7. Watkins, R. N. Sizing separators and accumulators. Hydrocarbon Process. 1967, 46 (11), 253-256.
8. Ludwig, E. E. Applied Process Design for Chemical and Petrochemical Plants; Gulf Publishing Co.: Houston, TX, 1977; Vol. 1.
9. Harriott, P. Process Control; McGraw-Hill: New York, 1964.
10. Hiester, A.; Melsheimer, S.; Vogel, E. Optimum size and location of surge capacity in continuous chemical processes. AlChe Annual Meeting, Nov 15-20, 1987; Paper 86c.
11. Marlin, T. E. Process Control. Designing Processes and Control Systems for Dynamic Performance; McGraw-Hill: New York, 1995.
12. Buckley, P. S. Techniques of Process Control; John Wiley & Sons, Inc.: New York, 1964.
13. McDonald, K. A.; McAvoy, T. J.; Tits, A. Optimal averaging level control. AlChE J. 1986, 32 (1), 75-86.
14. Shunta, J. P.; Fehervari, W. Nonlinear control of liquid level. Instrum. Technol. 1976, Jan, 43-48.
15. Shinskey, F. G. Process Control Systems-Application, Design, and Tuning, 4th ed.; McGraw-Hill Inc.: New York, 1996.
16. Shinskey, F. G. pH and pIon Control in Process and Waste Streams; John Wiley & Sons: New York, 1973.
17. McMillan, G. K. pH Control; Instrument Society of America: Research Triangle Park, NC, 1984.
18. Walsh, S. Integrated Design of Chemical Waste water Treatment Systems. Ph.D. Thesis, Imperial College, London, U.K., 1993.
19. Faanes, A.; Skogestad, S. pH-neutralization: Integrated process and control design. Comput. Chem. Eng. 2002, submitted for publication.
20. Zheng, A.; Mahajanam, R. V. A quantitative controllability index. Ind. Eng. Chem. Res. 1999, 38, 999-1006.
21. Skogestad, S.; Postlethwaite, I. Multivariable Feedback Control; John Wiley & Sons: New York, 1996.
22. Skogestad, S. Simple analytic rules for model reduction and PID controller tuning. J. Process Control 2003, 13 (4), 291-309.
23. Schei, T. S. Automatic tuning of PID controllers based on transfer function estimation. Automatica 1994, 30 (12), 1983-1989.