Control of the Neutralization Process with the Generic Model Algorithm
This paper is concerned with the application of the GMC control algorithm to a pilot plant for the neutralization process of a strong acid‐strong base system. A comparison of the experimental results for GMC with the conventional PI strategy is presented. The stability of GMC is analyzed for the neu...
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| Published in | Chemical engineering & technology Vol. 21; no. 4; pp. 369 - 376 |
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| Main Authors | , , |
| Format | Journal Article |
| Language | English |
| Published |
Weinheim
WILEY-VCH Verlag
01.04.1998
WILEY‐VCH Verlag Wiley-VCH |
| Subjects | |
| Online Access | Get full text |
| ISSN | 0930-7516 1521-4125 |
| DOI | 10.1002/(SICI)1521-4125(199804)21:4<369::AID-CEAT369>3.0.CO;2-1 |
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| Abstract | This paper is concerned with the application of the GMC control algorithm to a pilot plant for the neutralization process of a strong acid‐strong base system. A comparison of the experimental results for GMC with the conventional PI strategy is presented. The stability of GMC is analyzed for the neutralization process using the structured singular value concept.
The control of the neutralization process has been studied for several decades but it still remains a challenging problem from a practical point of view. The main difficult problem consists of the severe nonlinearity reflected in the S‐shaped gain curve of the system. Different models and control algorithms have been developed. However, most attempts have proved to be inadequate for practical application. |
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| AbstractList | This paper is concerned with the application of the GMC control algorithm to a pilot plant for the neutralization process of a strong acid‐strong base system. A comparison of the experimental results for GMC with the conventional PI strategy is presented. The stability of GMC is analyzed for the neutralization process using the structured singular value concept.
The control of the neutralization process has been studied for several decades but it still remains a challenging problem from a practical point of view. The main difficult problem consists of the severe nonlinearity reflected in the S‐shaped gain curve of the system. Different models and control algorithms have been developed. However, most attempts have proved to be inadequate for practical application. |
| Author | Manzi, Joao T. Odloak, Darci Langer, Otto-Ulrich |
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| Copyright | 1998 WILEY‐VCH Verlag GmbH, Weinheim, Fed. Rep. of Germany 1998 INIST-CNRS |
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| Issue | 4 |
| Keywords | Pilot plant Stability Process control Non linear control Strong acid Continuous stirred tank reactor Strong base Hydrochloric acid Genetic algorithm Sodium Hydroxides pH Singular value decomposition Neutralization |
| Language | English |
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| References_xml | – reference: Morari, M.; Zafirou, E., Robust Process Control, Prentice-Hall, Englewood Cliffs, NJ 1989. – reference: Lee, P. L.; Sullivan, G. R.; Zhou, W., Chem. Engng. Commun. 80 (1989) pp. 33-51. – reference: Dunia, R.; Edgar, T. F., Computers Chem. Engng. 20 (1996) pp. 1003-1016. – reference: Gustafsson, T. K.; Waller, K. V., Chem. Eng. Sci. 38 (1983) pp. 389-398. – reference: Lee, P. L.; Sullivan, G. R., Computers Chem. Engng. 12 (1988) pp. 573-580. – reference: McAvoy, T. J.; Hsu, E., Lowenthal, S., Ind. Eng. Chem. Process Des. Develop. 11 (1972) No. 1, pp. 68-70. – reference: Zames, G., IEEE Transactions on Automatic Control. 11 (1966) pp. 228-238. – reference: Williams, G. L.; Rhinehart, R. R.; Riggs, J. B., Ind. Eng. Chem. Res. 29 (1990) pp. 1254-1259. – reference: Lee, P. L.; Newell, R. B.; Sullivan, G. R., Canadian J Chem. Eng. 67 (1989) pp. 478-484. – reference: Waller, K. V.; Mäkilä, Ind. Eng. Chem., Process Des. Dev. 20 (1981) pp. 1-11. – reference: Bartusiak, R. D.; Georgakis, C.; Reily, M. J., Chem. Engng. Sci. 44 (1989) pp. 1837-1851. – reference: Costello, D. J.; Lee, P. L.; Greenfield, P. F., Bioprocesss Eng. 4 (1989) pp. 119-122. – reference: Mellichamp, D. A.; Coughanowr, D. R.; Koppel, L. B., A.I.Ch.E. J. 12 (1966) No. 1, pp. 75-82. – reference: Packard, A.; Doyle, J. C., Automatica 29 (1993) pp. 71-109. – volume: 29 start-page: 71 year: 1993 end-page: 109 publication-title: Automatica – volume: 29 start-page: 1254 year: 1990 end-page: 1259 publication-title: Ind. Eng. Chem. Res. – start-page: 349 year: 1992 end-page: 354 – volume: 67 start-page: 478 year: 1989 end-page: 484 publication-title: Canadian J Chem. Eng. – volume: 20 start-page: 1003 year: 1996 end-page: 1016 publication-title: Computers Chem. Engng. – volume: 38 start-page: 389 year: 1983 end-page: 398 publication-title: Chem. Eng. Sci. – year: 1989 – volume: 44 start-page: 1837 year: 1989 end-page: 1851 publication-title: Chem. Engng. Sci. – volume: 80 start-page: 33 year: 1989 end-page: 51 publication-title: Chem. Engng. Commun. – volume: 12 start-page: 573 year: 1988 end-page: 580 publication-title: Computers Chem. Engng. – volume: 20 start-page: 1 year: 1981 end-page: 11 publication-title: Ind. Eng. Chem., Process Des. Dev. – volume: 11 start-page: 228 year: 1966 end-page: 238 publication-title: IEEE Transactions on Automatic Control. – volume: 12 start-page: 75 issue: 1 year: 1966 end-page: 82 publication-title: A.I.Ch.E. J. – volume: 4 start-page: 119 year: 1989 end-page: 122 publication-title: Bioprocesss Eng. – volume: 11 start-page: 68 issue: 1 year: 1972 end-page: 70 publication-title: Ind. Eng. Chem. Process Des. Develop. |
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| Title | Control of the Neutralization Process with the Generic Model Algorithm |
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