Sammenlign metoder

	PFR-model	Adsorptionsisoterm (Langmuir-Freundlich)	Reaktiv destillation
Fagområde	Anvendt fysik	Anvendt fysik	Anvendt fysik
Familie	Process / pipeline	Process / pipeline	Process / pipeline
Oprindelsesår	1962	1918	1995
Ophavsperson	Octave Levenspiel	Irving Langmuir	Klaus Sundmacher
Type	Mathematical model for plug-flow reactor	Empirical and theoretical adsorption equilibrium model	Integrated reaction-separation process model
Oprindelig kilde	Levenspiel, O. (1999). Chemical Reaction Engineering (3rd ed.). John Wiley & Sons. ISBN: 978-0-471-25424-9	Langmuir, I. (1918). The adsorption of gases on plane surfaces of glass, mica, and platinum. Journal of the American Chemical Society, 40(9), 1361-1403.	Sundmacher, K., & Kienle, A. (2003). Reactive Distillation: Status and Future Directions. Wiley-VCH. ISBN: 978-3-527-30623-9
Aliasser	ideal tubular reactor, plug-flow model, PFR	Langmuir isotherm, Freundlich isotherm, sorption equilibrium	integrated distillation-reaction, reactive column, reaction with separation
Relaterede	3	3	4
Resumé	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.	Adsorption isotherms describe the equilibrium uptake of a substance on a solid surface as a function of gas or solution phase concentration at constant temperature. The Langmuir isotherm (1918) and Freundlich isotherm (1906) are classical empirical models. The Langmuir model assumes monolayer coverage and is mechanistic; the Freundlich model is empirical and describes multilayer or heterogeneous adsorption. These isotherms are essential for designing separation processes (activated carbon filters, molecular sieves) and understanding pollutant sorption.	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.