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Contents: VLE Basic terms Flash Distillation Steam Distillation Batch Distillation Multistage fractionation of binary mixtures McCabe Thiele Method Ponchon Savarit Azeotropic Distillation Extractive Distillation Reactive Distillation Conclusion
Vapour Liquid Equilibrium :
Constant T vapour liquid equilibria
Constant P vapour liquid equilibria
Raoult’s law:
For ideal is = 1.
•(+) ve deviation >1•(-) ve deviation <1•Azeotropes
Basic Terms:
Distillation Column Terms:
Relative volatilityCondenserReboilerDistillateBottomFeedLiquid RefluxRectifying sectionStripping section
Steam Distillation :The property of an immiscible liquid mixture forms the basis of steam
distillation.Case 1 – Substance A is immiscible with water and feed contains A and some traces of non volatile impurities .
If system is not at equilibrium than
E – Vaporizing efficiency
Case 2 – The feed is a mixture of A and C ; C is an essentially non volatile substance, A and C form an ideal solution and are immiscible with water.
;
Azeotropic distillation :
Azeotropic distillation of acetic acid water with butyl acetate.
Here butyl acetate is entrainer.
Advantages of RD :1. Single column replaces one reactor and 3 distillation
columns which is process integration.2. Less material is required for the construction of just
single column hence RD is much more cheap. Statistically, RD reduces about 50% of the cost as compared to conventional process.
3. Low energy consumption.4. Lower operating cost .
Disadvantages of RD :5. Degree of freedom is 3 for RD but for conventional
process it is 9. Hence conventional process gives us more variables than RD.
6. Above mentioned volatility problem is also a disadvantage. It limits it to very few reactions.
7. In some processes the optimum conditions of temperature and pressure for distillation may be far from optimal for reaction and vice versa.
Conclusion:
There are many methods to separate various mixtures . Maximizing the product by using minimum amount of investment is our final aim.