On the steady-state behaviour of the autocatalator model A + 2B⇌3B, B⇌C in a continuous-flow stirred-tank reactor

The steady-state behaviour of the ‘ autocatalator ’ model A + 2B⇌3B B⇌C in a continuous-flow stirred-tank reactor (CSTR) with flow rate as the bifurcation variable is investigated. It is shown that the model gives rise to a structurally stable singularity provided none of the rate constants is zero and all the species are present in the feed stream. When the inlet concentration of species A is greater than three times that of species C, there exist 14 stable bifurcation diagrams. Some of these bifurcation diagrams contain three different ranges of flow rates in which multiplicity exists. When the inlet concentration of species A is smaller than three times that of C, the organizing centre for the autocatalator is a winged cusp. The unfolding of this singularity gives seven stable bifurcation diagrams, which also exist for the physical system. In this case, the behaviour of the autocatalator is qualitatively the same as that of the classical problem of a single exothermic reaction in a CSTR.

2009 ◽  
Vol 11 (36) ◽  
pp. 7885 ◽  
Author(s):  
Dung L. Che ◽  
Jared D. Smith ◽  
Stephen R. Leone ◽  
Musahid Ahmed ◽  
Kevin R. Wilson

1997 ◽  
Vol 30 (4) ◽  
pp. 271-274 ◽  
Author(s):  
J.A. Bagshaw ◽  
Malcolm F. Fox ◽  
C.J. Jones ◽  
D.James Picken ◽  
Karl D.R. Seare

Author(s):  
Harsh Goud ◽  
Pankaj Swarnkar

AbstractModelling and controlling of Continuous stirred tank reactor (CSTR) is one of the major problems in the process industry. The nonlinear characteristic of CSTR may change the variation of temperature in either direction from the given set value. Chemical reactions within the CSTR depends on the given reference temperature. Such variation from reference values may result in degrading the variety of biomass. Design and implementation of the precise control device in such system are difficult for researchers. This paper proposes the MIT based control scheme as a solution to control problem of CSTR. An improvement of signal synthesis MIT system has been proposed in this study to enhance the steady-state and transient performance of CSTR. Artificial Bee Colony (ABC) based controller parameter tuning technique is applied to get the optimal performance of the controller. This paper shows the design and implementation of conventional PID tuned with the Z-N method, adaptive PID tune with ABC, MIT and ABC-MIT for CSTR. Detailed comparison based on simulation studies is presented which shows that ABC-MIT based control scheme improves the transient and steady state response.


2018 ◽  
Vol 3 (3) ◽  
pp. 333-343
Author(s):  
Sourav Sengupta ◽  
Amit Jain ◽  
Sirshendu De

The depectinization kinetics of bael (Aegle marmelos) juice using the enzyme pectinase was evaluated and it was observed to follow the Michaelis–Menten model.


1950 ◽  
Vol 42 (5) ◽  
pp. 817-825 ◽  
Author(s):  
Donald R. Mason ◽  
Edgar L. Piret

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