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Separation Columns (Distillation and absorption)
Dr. Kh. Nasrifar Department of Chemical and Petrochemical Engineering
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Importance and industrial relevance of azeotropic distillation
• Need for efficient recovery and recycle of organic solvents in chemical industry • Most liquid mixtures of organic solvents form azeotropes that complicate the synthesis and conceptual design of recovery processes • Distillation is the most common unit operation in recovery processes because of its ability to produce high purity products • Azeotropes make separation impossible by normal distillation but can be also utilised to separate mixtures not ordinarily separable by normal distillation • Azeotropic mixtures may often be effectively separated by distillation by adding a third component, called entrainer • Thus, knowledge of the limitations and possibilities in azeotropic distillation is a topic of great practical and industrial interest
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Terminology • The methods and tools presented in this lecture also appply for: − Azeotropic mixtures − Close boiling systems − Low relative volatility systems • Original components A and B: The components that form the azeotrope and need to be separated • Entrainer: A third component (E or C) added to enhance separation • Binary azeotrope: Azeotrope formed by two components • Ternary azeotrope: Azeotrope formed by three components • Homogeneous azeotrope: Azeotrope where the forming components are miscible • Heterogeneous azeotrope: Azeotrope where the forming components are immiscible
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Overview: Azeotropic distillation methods
i) Pressure swing distillation ii) Hybrid methods (membrane + distillation) iii) Homogeneous azeotropic (homoazeotropic) distillation iv) Heterogeneous azeotropic (heteroazeotropic) distillation v) Extractive distillation
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