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Simulation of hydrodynamic behaviour and mass transfer efficiency of reduced pressure distillation

Identifieur interne : 001050 ( Main/Exploration ); précédent : 001049; suivant : 001051

Simulation of hydrodynamic behaviour and mass transfer efficiency of reduced pressure distillation

Auteurs : N. Benadda [France] ; N. Moszkowicz [France] ; N. Prost [France] ; N. Otterbein [France] ; Kamal Mohammedi [Algérie]

Source :

RBID : ISTEX:FA5D2DC47B9187D39A86E6A13D04703ECA1A45C5

Abstract

A random packing hydrodynamic simulator is designed specially to carry out experiments under reduced pressures with a counter‐current flow air/water system. The simulator results (air/water system) compared to those obtained in a real packed distillation column (benzylchloride/ ethylbenzene system) show a good agreement between hydrodynamic parameters like pressure drop, flooding flow rate, and total liquid hold‐up. Empirical relationships derived from the simulator experimental results are proposed allowing the calculation of the pressure drop in a packed distillation column, operating in the pressure range between 10 kPa and atmospheric pressure. The influence of reduced pressure on the HETP in the distillation column and interfacial area in the simulator was also investigated.

Url:
DOI: 10.1002/ceat.270190404


Affiliations:


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