2005
DOI: 10.1021/ie049443s
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Multiple-Steady-States Identification in Homogeneous Azeotropic Distillation Using a Process Simulator

Abstract: Homogeneous azeotropic distillation processes may exhibit multiple steady states under certain conditions. A methodology has been described for directly capturing all the multiple steady states as well as for generating the bifurcation diagram using the HYSYS process simulator in the steady-state mode. Initial guesses for generating the multiple steady states were based on the ∞/∞ approach of Bekiaris et al. (Ind. Eng. Chem. Res. 1993, 32, 2023) and the behavior of the composition−temperature profiles. The met… Show more

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Cited by 11 publications
(17 citation statements)
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“…Both the conventional inside-out procedure [15] and the simultaneous correction procedure [57] were reported to miss the unstable steady-state solution, see [85] and [46] (all input variables specified; output multiplicity). However, all steady-state branches were computed either with the AUTO software package [20] or with an appropriate continuation method [39,46,85].…”
Section: Published Numerical Results With Continuation Methodsmentioning
confidence: 99%
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“…Both the conventional inside-out procedure [15] and the simultaneous correction procedure [57] were reported to miss the unstable steady-state solution, see [85] and [46] (all input variables specified; output multiplicity). However, all steady-state branches were computed either with the AUTO software package [20] or with an appropriate continuation method [39,46,85].…”
Section: Published Numerical Results With Continuation Methodsmentioning
confidence: 99%
“…However, all steady-state branches were computed either with the AUTO software package [20] or with an appropriate continuation method [39,46,85]. The initial estimates were carefully chosen with the ∞/∞ analysis [14,38], and special attention was paid to the turning points and branch switching.…”
Section: Published Numerical Results With Continuation Methodsmentioning
confidence: 99%
“…As for the simulation, conventional inside‐out12 and simultaneous correction13 procedures were reported to miss14, 15 the unstable steady‐state solution. In contrast, the general‐purpose solver IPOPT is able to converge to the unstable steady‐state solution from a poor starting point (given in mss2029).…”
Section: Resultsmentioning
confidence: 99%
“…Conventional inside‐out12 and simultaneous correction13 procedures were reported to miss14, 15 the unstable steady state solution of a homogeneous ternary azeotropic distillation problem (all input variables were specified; output multiplicity). All steady‐state branches were computed with an appropriate continuation method 14–17. A solution path was traced with respect to a user‐selected parameter (bifurcation parameter).…”
Section: Introductionmentioning
confidence: 99%
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