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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| Acceso en línea: | http://hdl.handle.net/20.500.12110/paper_09218610_v12_nC_p493_Cassanello |
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todo:paper_09218610_v12_nC_p493_Cassanello2023-10-03T15:45:43Z Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling Cassanello, M. Larachi, F. Laurent, A. Wild, G. Midoux, N. 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 evaluation of a and kLa at high pressure, and various liquid viscosities and packing characteristics. A simple model to estimate a and kLa for the low interaction regime in high pressure trickle-bed reactors is proposed. © 1996 Elsevier B.V. All rights reserved. Fil:Cassanello, M. Universidad de Buenos Aires. Facultad de Ciencias Exactas y Naturales; Argentina. SER info:eu-repo/semantics/openAccess http://creativecommons.org/licenses/by/2.5/ar http://hdl.handle.net/20.500.12110/paper_09218610_v12_nC_p493_Cassanello |
| institution |
Universidad de Buenos Aires |
| institution_str |
I-28 |
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R-134 |
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Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA) |
| description |
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 evaluation of a and kLa at high pressure, and various liquid viscosities and packing characteristics. A simple model to estimate a and kLa for the low interaction regime in high pressure trickle-bed reactors is proposed. © 1996 Elsevier B.V. All rights reserved. |
| format |
SER |
| author |
Cassanello, M. Larachi, F. Laurent, A. Wild, G. Midoux, N. |
| spellingShingle |
Cassanello, M. Larachi, F. Laurent, A. Wild, G. Midoux, N. Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling |
| author_facet |
Cassanello, M. Larachi, F. Laurent, A. Wild, G. Midoux, N. |
| author_sort |
Cassanello, M. |
| title |
Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling |
| title_short |
Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling |
| title_full |
Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling |
| title_fullStr |
Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling |
| title_full_unstemmed |
Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling |
| title_sort |
gas-liquid mass transfer in high pressure trickle-bed reactors: experiments and modelling |
| url |
http://hdl.handle.net/20.500.12110/paper_09218610_v12_nC_p493_Cassanello |
| work_keys_str_mv |
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1782024121109970944 |