Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale

This work analyzes the influence of liquid flow modulation on the behavior of a reaction occurring in a spherical porous particle within a trickle bed reactor. A single first-order reaction between a gaseous reactant and a non-volatile liquid reactant is considered. Non-steady-state mass balances fo...

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Autores principales: Ayude, María Alejandra, Cassanello Fernández, Miryam Celeste
Publicado: 2005
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Acceso en línea:https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_00092509_v60_n22_p6262_Ayude
http://hdl.handle.net/20.500.12110/paper_00092509_v60_n22_p6262_Ayude
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spelling paper:paper_00092509_v60_n22_p6262_Ayude2023-06-08T14:33:35Z Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale Ayude, María Alejandra Cassanello Fernández, Miryam Celeste Chemical reactors Liquid flow modulation Mathematical model Multiphase reactions Transient response Trickle bed reactors Mass transportation Porous materials Reaction kinetics Liquid flow modulation Reaction rate Trickle bed reactors Chemical reactors liquid flow mathematical modeling trickle bed reactor This work analyzes the influence of liquid flow modulation on the behavior of a reaction occurring in a spherical porous particle within a trickle bed reactor. A single first-order reaction between a gaseous reactant and a non-volatile liquid reactant is considered. Non-steady-state mass balances for gas and liquid reactants are formulated and solved under isothermal conditions in order to focus the analysis on the mass transport effects. Dynamic reactant profiles inside the catalytic particle are obtained for different cycling and system conditions. The enhancement factor (ε) due to periodic operation is defined to evaluate the impact of induced liquid flow modulation on reaction rate. Influence of cycling and system parameters on the enhancement factor is also reported for a wide range of conditions. Experimental trends observed by several authors can be explained with this approach. © 2005 Elsevier Ltd. All rights reserved. Fil:Ayude, M.A. Universidad de Buenos Aires. Facultad de Ciencias Exactas y Naturales; Argentina. Fil:Cassanello, M.C. Universidad de Buenos Aires. Facultad de Ciencias Exactas y Naturales; Argentina. 2005 https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_00092509_v60_n22_p6262_Ayude http://hdl.handle.net/20.500.12110/paper_00092509_v60_n22_p6262_Ayude
institution Universidad de Buenos Aires
institution_str I-28
repository_str R-134
collection Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA)
topic Chemical reactors
Liquid flow modulation
Mathematical model
Multiphase reactions
Transient response
Trickle bed reactors
Mass transportation
Porous materials
Reaction kinetics
Liquid flow modulation
Reaction rate
Trickle bed reactors
Chemical reactors
liquid flow
mathematical modeling
trickle bed reactor
spellingShingle Chemical reactors
Liquid flow modulation
Mathematical model
Multiphase reactions
Transient response
Trickle bed reactors
Mass transportation
Porous materials
Reaction kinetics
Liquid flow modulation
Reaction rate
Trickle bed reactors
Chemical reactors
liquid flow
mathematical modeling
trickle bed reactor
Ayude, María Alejandra
Cassanello Fernández, Miryam Celeste
Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale
topic_facet Chemical reactors
Liquid flow modulation
Mathematical model
Multiphase reactions
Transient response
Trickle bed reactors
Mass transportation
Porous materials
Reaction kinetics
Liquid flow modulation
Reaction rate
Trickle bed reactors
Chemical reactors
liquid flow
mathematical modeling
trickle bed reactor
description This work analyzes the influence of liquid flow modulation on the behavior of a reaction occurring in a spherical porous particle within a trickle bed reactor. A single first-order reaction between a gaseous reactant and a non-volatile liquid reactant is considered. Non-steady-state mass balances for gas and liquid reactants are formulated and solved under isothermal conditions in order to focus the analysis on the mass transport effects. Dynamic reactant profiles inside the catalytic particle are obtained for different cycling and system conditions. The enhancement factor (ε) due to periodic operation is defined to evaluate the impact of induced liquid flow modulation on reaction rate. Influence of cycling and system parameters on the enhancement factor is also reported for a wide range of conditions. Experimental trends observed by several authors can be explained with this approach. © 2005 Elsevier Ltd. All rights reserved.
author Ayude, María Alejandra
Cassanello Fernández, Miryam Celeste
author_facet Ayude, María Alejandra
Cassanello Fernández, Miryam Celeste
author_sort Ayude, María Alejandra
title Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale
title_short Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale
title_full Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale
title_fullStr Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale
title_full_unstemmed Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale
title_sort phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale
publishDate 2005
url https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_00092509_v60_n22_p6262_Ayude
http://hdl.handle.net/20.500.12110/paper_00092509_v60_n22_p6262_Ayude
work_keys_str_mv AT ayudemariaalejandra phenomenologicalapproachtointerprettheeffectofliquidflowmodulationintricklebedreactorsattheparticlescale
AT cassanellofernandezmiryamceleste phenomenologicalapproachtointerprettheeffectofliquidflowmodulationintricklebedreactorsattheparticlescale
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