Axial mixing models. Height of differential devices
Liquid-liquid extraction - Column modeling
Article REF: J2765 V1
Axial mixing models. Height of differential devices
Liquid-liquid extraction - Column modeling

Author : Jean LEYBROS

Publication date: September 10, 2004 | Lire en français

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

Already subscribed?

4. Axial mixing models. Height of differential devices

4.1 Type of axial mixture

The study of mixing phenomena is of great importance for the calculation of chemical reactors, and has been considerably developed in this field. In the case of a transfer operation, the problem is made more complex by the presence of a dispersed phase whose behavior is different from that of the continuous phase.

  • Mixing of the continuous phase remains analogous to that observed in single-phase flow. Velocity distribution may deviate from a uniform distribution due to the existence of stagnant zones or preferential paths

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
Axial mixing models. Height of differential devices

Article included in this offer

"Unit operations. Chemical reaction engineering"

( 338 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