Classification of New Product changeover Strategy (NPS) for different application of distillation columns

Computers and Chemical Engineering

Volumn 20, Issue SUPPL.2, 1996, Pages

  Flender, M ^a   Fieg, G ^b   Wozny, G ^a  

^a TECHNISCHE UNIVERSITÄT BERLIN   (Germany)

^b HENKEL KGAA   (Germany)

Author keywords

[No Author keywords available]

Indexed keywords

DISTILLATION COLUMNS; PRODUCTION METHODS;

FLOWCHARTING; MATHEMATICAL MODELS; OPERATIONS RESEARCH; OPTIMIZATION; PROCESS CONTROL; TIME VARYING CONTROL SYSTEMS;

DISTILLATION COLUMNS;

EID: 0029657107     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/0098-1354(96)00196-2     Document Type: Article

References (6)

1. Kruse, C./ Fieg, G./ Wozny, G.: "A new time-optimal strategy for column startup and product changeover", Fith International Symposium on Process Systems Engineering, Seoul 1994.
2. Kruse, C./ Fieg, G./ Wozny, G.: "Experimental and theoretical studies of the dynamics of startup and product switchover operations of distillation columns", Chem. Eng. Processing, 32, (1993), 283-290.
3. Jacobsen, E. W./ Skogestad, S.: "Dynamics and Control of Unstable Distillation Columns", IFAC 1992, Maryland.
4. Lüder, T.: "Ein Automatisierungskonzept für Rektifikationskolonnen auf der Basis der dynamischen Modellbildung", VDI-Verlag, Reihe 8: Meß-, Steuerungs- und Regelungstechnik Nr. 310, 1992.
5. Yasuoka, H.: "A convenient algorithm for the on-line optimum startup operation of binary distillation columns",Memoirs of the faculty of Engineering Kobe university, 29, (1982), 161-169.
6. Barolo, M./ Guarise, G./ Rienzi, S./ Trotta, A./: "On-line startup of distillation column using generic model control".ESCAPE-2, Toulouse 1992.