A Multivariable Model Predictive Controller (MVPC) is applied at the coordinating control level. The design and application of the MVPC is introduced and demonstrated. A well structured, first principle dynamic model was developed for the regenerator/reactor section of a FCC plant. The control exper
Fluid catalytic cracking unit advanced control in a distributed control system
β Scribed by A.H. Timbalia; R.B. Butterfield; D.W. Webb; Jim Hiebert
- Publisher
- Elsevier Science
- Year
- 1991
- Tongue
- English
- Weight
- 730 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0019-0578
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optimum polynomial quotient S'/d (S': variance of fit; 2. variance of experimental values). the multicorrelation coefficient M R . and a Chi' test. [4] C. A. Tolman. Chem. Rev. 77. 313 (1977): the "electronic" parameter x, of the ligand L, is determined by IR spectroscopy ria the induced shlft of t
In this article we describe our experience in integration of the chemical engineering unit operations laboratory using an industrial distributed control system (DCS). We discuss the positive effect that the new control and data acquisition technology has on our curriculum, and outline some direction