Multiple steady states in a CSTR with total condenser: Comparison of equilibrium and nonequilibrium models
Keyword(s):
Start Up
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AbstractComparison of equilibrium and nonequilibrium models of a CSTR with total condenser focused on the multiple steady states and dynamic behaviour was carried out. The steady-state behaviour of the model system, MTBE synthesis from methanol and isobutene in a reactive distillation column, was studied in terms of the input parameters, i. e. feed flow rate of methanol or butenes, reflux ratio, and mass of catalyst. The dynamic behaviour of the system during the start-up was investigated and perturbations of manipulated variables were found to cause transitions between the parallel steady states.
2008 ◽
Vol 80
(5)
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pp. 865-881
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1998 ◽
Vol 21
(2)
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pp. 133-136
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Keyword(s):
1998 ◽
Vol 21
(2)
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pp. 136-139
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2010 ◽
Vol 34
(4)
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pp. 460-466
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2012 ◽
Vol 468-471
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pp. 2785-2789
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1993 ◽
Vol 32
(11)
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pp. 2767-2774
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2014 ◽
Vol 40
(3)
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pp. 244-249
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