Distillation with pressure change
Distillation of non-ideal mixtures

Add to my library

J2612 V1 Article

Distillation with pressure change
Distillation of non-ideal mixtures

Authors : Vincent GERBAUD, Ivonne RODRIGUEZ-DONIS

Review date: March 1, 2015 | Lire en français

Add to my library Add to my library

Logo Techniques de l'Ingenieur You do not have access to this resource.
Request your free trial access! Free trial

Already subscribed?

3. Distillation with pressure change

If the composition of the azeotrope AzAB or the relative volatility αAB varies with pressure, a conventional distillation process can be used, introducing no entrainer, which therefore needs neither vaporization nor recovery.

Generally, the composition of the light component A in the azeotropic mixture increases as the pressure decreases, possibly until the azeotrope disappears.

Thus, for the homoazeotrope Tmax water (100 °C) – formic acid (100.8 °C),

xwater = 0.42 at 1 atm (760 mmHg) (Tazeo = 107.3 °C),

xwater = 0.50 to 0.26 atm (200 mmHg) (Tazeo = 71.3 °C),

xwater = 0.58 at 0.13 atm (100 mmHg) (Tazeo = 55.7 °C).

For water-ethanol, the azeotrope disappears below 0.07 atm.

In the pressure-swing distillation process,...

You do not have access to this resource.
Logo Techniques de l'Ingenieur

Exclusive to subscribers. 97% yet to be discovered!

You do not have access to this resource. Click here to request your free trial access!

Already subscribed?


Ongoing reading
Distillation with pressure change

Article included in this offer

"Unit operations. Chemical reaction engineering"

( 343 articles )

Complete knowledge base

Updated and enriched with articles validated by our scientific committees

Services

A set of exclusive tools to complement the resources

View offer details
Contact us