เปรียบเทียบวิธี

	ไอโซเทอร์มการดูดซับ (Langmuir-Freundlich)	แบบจำลอง CSTR	การกลั่นแบบเกิดปฏิกิริยา
สาขาวิชา	ฟิสิกส์ประยุกต์	ฟิสิกส์ประยุกต์	ฟิสิกส์ประยุกต์
ตระกูล	Process / pipeline	Process / pipeline	Process / pipeline
ปีกำเนิด	1918	1962	1995
ผู้ริเริ่ม	Irving Langmuir	Octave Levenspiel	Klaus Sundmacher
ประเภท	Empirical and theoretical adsorption equilibrium model	Mathematical model for continuous flow reactor	Integrated reaction-separation process model
แหล่งต้นตำรับ	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.	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
ชื่อเรียกอื่น	Langmuir isotherm, Freundlich isotherm, sorption equilibrium	ideal mixed reactor, back-mix reactor, CSTR	integrated distillation-reaction, reactive column, reaction with separation
ที่เกี่ยวข้อง	3	3	4
สรุป	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.	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Reactor) model describes the behavior of an ideal mixed reactor where fresh feed is continuously added, products are withdrawn, and contents are kept uniform by vigorous stirring.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.	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.