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...
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| Autores principales: | Cassanello, M., Larachi, F., Laurent, A., Wild, G., Midoux, N. |
|---|---|
| Formato: | SER |
| Acceso en línea: | http://hdl.handle.net/20.500.12110/paper_09218610_v12_nC_p493_Cassanello |
| Aporte de: |
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