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Pressure Swing Distillation to Break Azeotropes

In Chemical Process Industries (CPI) we face the distillation problem of azeotropes or close boiling chemical mixtures. So, to break the azeotropes we can use several techniques like, azeotropic distillation using entrainers, extractive distillation using solvents, molecular sieves, and pressure sensitive distillation or PSD. However, we can find the use of first three methods in

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Steam Distillation Method for Component Separation

In chemical process industries, we can find the use of steam distillation method for many services. Mainly, we use this technique where we want to distil the components form high boiling point mixtures or altogether non-volatile salt solutions. For example, recovery of 2-chloropyridine from neutralized solution containing pyridine, NaCl and water. Moreover, steam distillation become

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Process Simulation of Anhydrous Alcohol Plant

As we know ethanol and water forms azeotropes and it is not possible to produce anhydrous alcohol by simple distillation process. So, due to this azeotrope formation we can purify ethanol up to 89 mole% only. Therefore, to get anhydrous alcohol we require different techniques like hydrophilic molecular sieves or azeotropic distillation. In this article

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Azeotropic Distillation Process for Ethanol Dehydration

In chemical process industries, we come across certain mixtures where separation is impossible or difficult by simple distillation. This type of mixtures we know by the name of azeotropic mixture. Other than this, if relative volatility of the mixture is close to 1.0, in the cases when components boiling points are very close, then also

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Data Sheets for Distillation Column

In chemical process industries we can see various types of columns. We use these columns for different unit operations like distillation, absorption, stripping, extraction and reaction also. Any column is a vertical cylindrical vessel having internals inside to enhance the contact surface area between phases. These phases can be liquid-gas, liquid-vapor, liquid-liquid. During process design

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