Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling
Gas-liquid interfacial areas a and volumetric liquid-side mass-transfer coefficients kLa are experimentally determined in a high pressure tri reactor up to 3.2 MPa. Fast and slow absorption of carbon dioxide in aqueous and organic diethanolamine solutions are employed as model reactions for the eval...
| Autor principal: | Cassanello Fernández, Miryam Celeste |
|---|---|
| Publicado: |
1996
|
| Acceso en línea: | https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_09218610_v12_nC_p493_Cassanello http://hdl.handle.net/20.500.12110/paper_09218610_v12_nC_p493_Cassanello |
| Aporte de: |
Ejemplares similares
-
Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling
por: Cassanello, M., et al. - Assessment of mass transfer in the stagnant liquid regions in trickle-bed reactors.
-
General criteria to analyze the role of mass transfer and hydrodynamics in trickle-bed reactors
por: Cassanello Fernández, Miryam Celeste, et al.
Publicado: (1996) -
Towards a comprehensive model for liquid flow modulation in trickle bed reactors
por: Ayude, María Alejandra, et al.
Publicado: (2009) -
Local solid-liquid mass transfer coefficients in a trickle bed reactor
por: Gabitto, Jorge Federico, et al.
Publicado: (1987)