Effect of control loop configuration on the bifurcation behavior and gasoline yield of industrial fluid catalytic cracking (FCC) units

DOI10.1016/S0895-7177(97)00014-9zbMath1002.92571MaRDI QIDQ1368487

S. S. E. H. Elnashaie, Khalid Alhumaizi

Publication date: 15 January 2003

Published in: Mathematical and Computer Modelling (Search for Journal in Brave)

zbMATH Keywords

stabilitydynamicsbifurcationfeedback controlFCCfluid catalytic cracking units

Mathematics Subject Classification ID

Classical flows, reactions, etc. in chemistry (92E20) Application models in control theory (93C95)

Related Items (4)

Chaos and bifurcation control of SSR in the IEEE second benchmark model ⋮ BIFURCATION CONTROL: THEORIES, METHODS, AND APPLICATIONS ⋮ Robust optimization of stiff delayed systems: application to a fluid catalytic cracking unit ⋮ Stabilization of chaotic behavior in a two-phase autocatalytic reactor

Uses Software

• AUTO
• AUTO-86

Cites Work

• Comparison between different mathematical models for the simulation of industrial fluid catalytic cracking (FCC) units
• Unnamed Item

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