Enhanced Distillation Techniques Recommended also for Pressure Swing

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Enhanced Distillation Techniques

Enhanced Distillation Techniques

(Recommended also for Pressure Swing & ED)

(Recommended also for Pressure Swing & ED)

Small deviation from Ideality Zeotropic System Large deviation from Ideality Azeotropic System

Small deviation from Ideality Zeotropic System Large deviation from Ideality Azeotropic System

Minimum-boiling Azeotrope Strong repulsive forces CS 2 -Acetone Positive Deviation

Minimum-boiling Azeotrope Strong repulsive forces CS 2 -Acetone Positive Deviation

Maximum-boiling Azeotrope Strong attractive forces HCL-Water 20%&80%, 80 & 100 o. C BP Azeotrope

Maximum-boiling Azeotrope Strong attractive forces HCL-Water 20%&80%, 80 & 100 o. C BP Azeotrope boils at 110 o. C Negative Deviation

Ø Maximum-boiling Azeotropes are not separated using Azeotropic Distillation due to high energy requirement

Ø Maximum-boiling Azeotropes are not separated using Azeotropic Distillation due to high energy requirement Ø Low-boiling Azeotropes can be separated using Azeotropic Distillation in two ways depending upon type of Entrainer: (a) Homogenous Low-boiling Azeotropic Distillation: In this distillation, Entrainer (E) breaks the azeotrope of feed (A&B) and form of new azeotrope (Entrainer+any one component of feed i. e. E&A) in distillation column. The E&A are available as a top product and B as a bottom Product. Here, E&A are miscible and has to be separated in next second distillation column. [EXTRA distillation & stripper columns are required for homogeneous solution of E&A] (b) Heterogeneous Low-boiling Azeotropic Distillation: In this distillation, Entrainer (E) breaks the azeotrope of feed (A&B) and form of new azeotrope (Entrainer+any one component of feed i. e. E&A) in distillation column. The E&A are available as a top product and B as a bottom Product. Here, E&A are immiscible so can be separated easily using decanter. [NO EXTRA distillation column is required for hetrogeneous solution of E&A]. In practice this type of Azeotropic Distillation is used due to economy.

Homogeneous AD: Benzene-Cyclohexane : 55&45%, Entrainer: 1 Butyl-3 -methylimidazolium thiocyanae For more examples of

Homogeneous AD: Benzene-Cyclohexane : 55&45%, Entrainer: 1 Butyl-3 -methylimidazolium thiocyanae For more examples of Azeotropes visit: https: //en. wikipedia. org/wiki/Azeotrope_tables

Ethanol BP = 78 o. C Heterogeneous Benzene BP = 80 o. C Ethanol-Water

Ethanol BP = 78 o. C Heterogeneous Benzene BP = 80 o. C Ethanol-Water Azeotrope @95. 67 -4. 37% Benzene-Water Azeotrope @91 -9% With BP 69 o. C, column 2 Benzene-Water Solubility : 1. 84 g/L (30 °C) 2. 26 g/L (61 °C) 3. 94 g/L (100 °C) Minimum BP Azeotropic Distillation

Extractive Distillation

Extractive Distillation

ED BP of PG 188 o. C

ED BP of PG 188 o. C

Salt Distillation One type of extractive distillation in which relative volatility of key components

Salt Distillation One type of extractive distillation in which relative volatility of key components is altered by dissolving a soluble SALT in the top reflux

VLE Salting out methanol by saturated aqueous sodium nitrate Salting out methanol by saturated

VLE Salting out methanol by saturated aqueous sodium nitrate Salting out methanol by saturated aqueous mercuric chloride : : Not Preferred

VLE Effect of salt concentration on ethanol-water equlibria

VLE Effect of salt concentration on ethanol-water equlibria

Pressure Swing Distillation

Pressure Swing Distillation

Ethylenediamine-water separation using PSD

Ethylenediamine-water separation using PSD

Reactive Distillation

Reactive Distillation

AST Sanjay Patel

AST Sanjay Patel

CA Membrane Very high permeability of methanol Commercial plant by Separex (UOP) 120 gallon/hr

CA Membrane Very high permeability of methanol Commercial plant by Separex (UOP) 120 gallon/hr AST Sanjay Patel MTBE Production using Pervaporation