Journal of the Chinese Institute of Engineers · 1990 · 12 citations · 14 references
EngineeringChemical EngineeringPhysical ChemistryProcess DynamicsReaction EngineeringContinuous Stirred-tank ReactorsGas-liquid ReactorsReactor ModelingContinuous Stirred-tank Reactor ModelingMultiple Steady StatesNon-equilibrium Steady StatesNon-ideal FlowNonideal FlowNonideal Flow ModelingPerfect Mixing ModelStirred Tank Reactor Design
Abstract In this paper, the problems of multiplicity and uniqueness of steady states in a nonadiabatic CSTR are discussed, using the Cholette's model. The result shows that the parameters m (the fraction of the total volume which is perfectly mixed) and n (the fraction of the feed entering the zone of perfect mixing) of Cholette's model seem to strongly determine the multiplicity and uniqueness region. When parameters m and n are changed, the exact region of multiplicity will be shifted. In addition, we derive the necessary and sufficient conditions for steady state multiplicity and uniqueness in the non‐ideal mixing of CSTR. As the non‐ideal mixing takes place in a real reactor, our results will be of significant use in chemical reactor design.
14
Dispersed phase mixing: I. Theory and effects in simple reactors
Rane L. Curl · AIChE Journal · 1963 · 598 citations
C. van Heerden · Industrial & Engineering Chemistry · 1953 · 306 citations