Sammenlign metoder

	CSTR-modell	PFR-modellen	Reaktiv destillasjon
Fagfelt	Anvendt fysikk	Anvendt fysikk	Anvendt fysikk
Familie	Process / pipeline	Process / pipeline	Process / pipeline
Opprinnelsesår	1962	1962	1995
Opphavsperson	Octave Levenspiel	Octave Levenspiel	Klaus Sundmacher
Type	Mathematical model for continuous flow reactor	Mathematical model for plug-flow reactor	Integrated reaction-separation process model
Opprinnelig kilde	Levenspiel, O. (1999). Chemical Reaction Engineering (3rd ed.). John Wiley & Sons. ISBN: 978-0-471-25424-9	Levenspiel, O. (1999). Chemical Reaction Engineering (3rd ed.). John Wiley & Sons. ISBN: 978-0-471-25424-9	Sundmacher, K., & Kienle, A. (2003). Reactive Distillation: Status and Future Directions. Wiley-VCH. ISBN: 978-3-527-30623-9
Alias	ideal mixed reactor, back-mix reactor, CSTR	ideal tubular reactor, plug-flow model, PFR	integrated distillation-reaction, reactive column, reaction with separation
Relaterte	3	3	4
Sammendrag	The CSTR (Continuous Stirred-Tank Reactor) model describes the behavior of an ideal mixed reactor where fresh feed is continuously added, products are withdrawn, and contents are kept uniform by vigorous stirring. This fundamental model, formalized by Octave Levenspiel in the 1960s, is widely used to design and scale batch and continuous processes. Despite its simplicity, it captures essential dynamics of industrial reactors and is the baseline for process control and optimization.	The PFR (Plug Flow Reactor) model describes the behavior of a tubular reactor in which fluid elements move through as distinct plugs with no axial mixing. Fluid at the inlet is freshly unreacted; as it travels downstream, reactions progress. This idealized model, formalized by Octave Levenspiel alongside CSTR theory, is the opposite extreme: while CSTRs are fully mixed, PFRs have no axial mixing. In practice, PFRs achieve higher conversion than CSTRs for the same residence time and are widely used in the chemical and petroleum industries.	Reactive distillation couples reaction and separation in a single column, where reactants are separated from products continuously while simultaneously undergoing reaction on catalytic trays. Pioneered in the 1990s by Klaus Sundmacher and others, this process intensification technique dramatically reduces capital cost, energy consumption, and environmental impact for suitable reactions. It is now industrially proven for esterification, hydration, and transesterification processes.