Instability of distillation columns

As recently recognized, distillation columns, operating with reflux and boilup as independent inputs, may have multiple steady‐state solutions, even in the ideal binary case. Two fundamentally different sources may cause the multiplicity, and in both cases some operating points are found to be unsta...

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Veröffentlicht in:	AIChE journal 1994-09, Vol.40 (9), p.1466-1478
Hauptverfasser:	Jacobsen, Elling W., Skogestad, Sigurd
Format:	Artikel
Sprache:	eng
Schlagworte:	02 PETROLEUM 020400 > Petroleum-- Processing Applied sciences Chemical engineering CONTROL Distillation DISTILLATION EQUIPMENT ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION EQUIPMENT 320303 > Energy Conservation, Consumption, & Utilization-- Industrial & Agricultural Processes-- Equipment & Processes Exact sciences and technology FLUID FLOW MATHEMATICAL MODELS OPERATION PROCESS CONTROL STABILITY
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