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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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
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Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA) de Universidad de Buenos Aires
id paper:paper_09218610_v12_nC_p493_Cassanello
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spelling paper:paper_09218610_v12_nC_p493_Cassanello2023-06-08T15:50:51Z Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling Cassanello Fernández, Miryam Celeste 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. 1996 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
institution Universidad de Buenos Aires
institution_str I-28
repository_str R-134
collection 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.
author Cassanello Fernández, Miryam Celeste
spellingShingle Cassanello Fernández, Miryam Celeste
Gas-liquid mass transfer in high pressure trickle-bed reactors: Experiments and modelling
author_facet Cassanello Fernández, Miryam Celeste
author_sort Cassanello Fernández, Miryam Celeste
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
publishDate 1996
url 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
work_keys_str_mv AT cassanellofernandezmiryamceleste gasliquidmasstransferinhighpressuretricklebedreactorsexperimentsandmodelling
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