Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale

The behavior of an isothermal catalytic particle in a TBR with ON-OFF liquid flow modulation has been modeled considering isothermal conditions. The impact of catalytic properties has been investigated considering uniform and egg shell distributions. Furthermore, the effect of varying inert core por...

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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_08885885_v44_n25_p9594_Ayude
http://hdl.handle.net/20.500.12110/paper_08885885_v44_n25_p9594_Ayude
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spelling paper:paper_08885885_v44_n25_p9594_Ayude2023-06-08T15:46:58Z Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale Ayude, María Alejandra Cassanello Fernández, Miryam Celeste Catalysts Industrial engineering Mathematical models Porosity Catalyst design Egg shell distributions Liquid flow modulation Trickle bed reactors Chemical reactors catalyst design trickle bed reactor The behavior of an isothermal catalytic particle in a TBR with ON-OFF liquid flow modulation has been modeled considering isothermal conditions. The impact of catalytic properties has been investigated considering uniform and egg shell distributions. Furthermore, the effect of varying inert core porosity for egg shell catalysts has also been addressed. The model represents experimental trends observed for slow and intermediate cycling. In most cases, egg shell catalysts presented a better performance in comparison with uniform catalysts. However, during cycling, performance depends on working conditions and catalytic properties. Therefore, catalyst design and mode of operation are related issues that need to be defined jointly. The relevance of internal processes (reaction, diffusion, and accumulation) and external transport on overall performance has been addressed. Therefore, the model would serve as a basis, coupled with the development at reactor scale, for the integral reactor design. © 2005 American Chemical Society. 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_08885885_v44_n25_p9594_Ayude http://hdl.handle.net/20.500.12110/paper_08885885_v44_n25_p9594_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 Catalysts
Industrial engineering
Mathematical models
Porosity
Catalyst design
Egg shell distributions
Liquid flow modulation
Trickle bed reactors
Chemical reactors
catalyst
design
trickle bed reactor
spellingShingle Catalysts
Industrial engineering
Mathematical models
Porosity
Catalyst design
Egg shell distributions
Liquid flow modulation
Trickle bed reactors
Chemical reactors
catalyst
design
trickle bed reactor
Ayude, María Alejandra
Cassanello Fernández, Miryam Celeste
Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale
topic_facet Catalysts
Industrial engineering
Mathematical models
Porosity
Catalyst design
Egg shell distributions
Liquid flow modulation
Trickle bed reactors
Chemical reactors
catalyst
design
trickle bed reactor
description The behavior of an isothermal catalytic particle in a TBR with ON-OFF liquid flow modulation has been modeled considering isothermal conditions. The impact of catalytic properties has been investigated considering uniform and egg shell distributions. Furthermore, the effect of varying inert core porosity for egg shell catalysts has also been addressed. The model represents experimental trends observed for slow and intermediate cycling. In most cases, egg shell catalysts presented a better performance in comparison with uniform catalysts. However, during cycling, performance depends on working conditions and catalytic properties. Therefore, catalyst design and mode of operation are related issues that need to be defined jointly. The relevance of internal processes (reaction, diffusion, and accumulation) and external transport on overall performance has been addressed. Therefore, the model would serve as a basis, coupled with the development at reactor scale, for the integral reactor design. © 2005 American Chemical Society.
author Ayude, María Alejandra
Cassanello Fernández, Miryam Celeste
author_facet Ayude, María Alejandra
Cassanello Fernández, Miryam Celeste
author_sort Ayude, María Alejandra
title Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale
title_short Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale
title_full Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale
title_fullStr Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale
title_full_unstemmed Periodic operation of trickle bed reactors: An approach to catalyst design through modeling at the particle scale
title_sort periodic operation of trickle bed reactors: an approach to catalyst design through modeling at the particle scale
publishDate 2005
url https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_08885885_v44_n25_p9594_Ayude
http://hdl.handle.net/20.500.12110/paper_08885885_v44_n25_p9594_Ayude
work_keys_str_mv AT ayudemariaalejandra periodicoperationoftricklebedreactorsanapproachtocatalystdesignthroughmodelingattheparticlescale
AT cassanellofernandezmiryamceleste periodicoperationoftricklebedreactorsanapproachtocatalystdesignthroughmodelingattheparticlescale
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