Dynamical and technological consequences of multiple isolas of steady states in a catalytic fluidised-bed reactor

Journal title

Chemical and Process Engineering




vol. 38


No 3


Divisions of PAS

Nauki Techniczne


Polish Academy of Sciences Committee of Chemical and Process Engineering




ISSN 0208-6425


Balakotaiah (2014), Thermal effects and bifurcations in catalytic partial oxidations, Curr Chem Eng, 68, ; Grace (2002), Abba Variable - gas - density fluidized bed reactor model for catalytic processes, Chem Eng Sci, 4797, ; Seydel (1994), Practical bifurcation and stability analysis From equilibrium to chaos Springer Verlag New York, null. ; Pinto (1995), The dynamic behavior of continuous solution polymerization reactors VIII full bifurcation analysis of a lab - scale copolymerization reactor, Chem Eng Sci, 1041, ; Tabiś (2001), Methanol synthesis in a fluidized - bed reactor coupled with an external heat exchanger The effect of feedback deformation, Chem Eng J, 191, ; Ajbar (2001), Classification of static and dynamic behaviour in a fluidized - bed catalytic reactor, Chem Eng J, 503, ; Westerink (1990), Stable design and operation of catalytic fluidized - bed reactors for multiple reactions Uniqueness multiplicity, Chem Eng J, 45, ; Berezowski (2010), The application of the parametric continuation method for determining steady state diagrams in chemical engineering, Chem Eng Sci, 65, ; Berezowski (2000), Method of determination of steady - state diagrams of chemical reactors, Chem Eng Sci, 55, ; Zahn (2012), Adiabatic simulated moving bed reactor principle nonlinear analysis and experimental demonstration Shaker Verlag GmbH Herzogenrath, null. ; Berezowski (2002), struktura stanów stacjonarnych układu równolegle połączonych reaktorów zbiornikowych, Chem Proc, 23, 415. ; Bizon (2016), multiplicity yield and selectivity of catalytic processes in a polytropic fluidized bed reactor, Chem Eng J, 288, ; Uppal (1976), The classification of the dynamic behavior of continuous stirred tank reactors - Influence of reactor residence time, Chem Eng Sci, 31, 205,