Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions

ABSTRACT: In the field of hydrocracking reactions, achieving optimal middle distillate yields remains a persistent challenge with commercially available zeolite Y catalysts. This limitation is attributed to challenges related to diffusion constraints within the catalyst. In response, we present a pr...

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Autores:
Mendoza Merlano, Carlos Javier
Manrique Hernández, Alba Cecilia
Echavarría Isaza, Adriana
Tipo de recurso:
Article of investigation
Fecha de publicación:
2024
Institución:
Universidad de Antioquia
Repositorio:
Repositorio UdeA
Idioma:
eng
OAI Identifier:
oai:bibliotecadigital.udea.edu.co:10495/44744
Acceso en línea:
https://hdl.handle.net/10495/44744
Palabra clave:
Catalizadores
Catalysts
Zeolitas
Zeolites
Lantano
Lanthanum
Reacciones químicas
Chemical reactions
Hidrocarburos
Hydrocarbons
Craqueo
Cracking process
Hidrogenación
Hydrogenation
Rights
openAccess
License
http://creativecommons.org/licenses/by-nc/2.5/co/
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oai_identifier_str oai:bibliotecadigital.udea.edu.co:10495/44744
network_acronym_str UDEA2
network_name_str Repositorio UdeA
repository_id_str
dc.title.spa.fl_str_mv Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
title Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
spellingShingle Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
Catalizadores
Catalysts
Zeolitas
Zeolites
Lantano
Lanthanum
Reacciones químicas
Chemical reactions
Hidrocarburos
Hydrocarbons
Craqueo
Cracking process
Hidrogenación
Hydrogenation
title_short Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
title_full Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
title_fullStr Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
title_full_unstemmed Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
title_sort Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions
dc.creator.fl_str_mv Mendoza Merlano, Carlos Javier
Manrique Hernández, Alba Cecilia
Echavarría Isaza, Adriana
dc.contributor.author.none.fl_str_mv Mendoza Merlano, Carlos Javier
Manrique Hernández, Alba Cecilia
Echavarría Isaza, Adriana
dc.contributor.researchgroup.spa.fl_str_mv Catalizadores y Adsorbentes
dc.subject.lemb.none.fl_str_mv Catalizadores
Catalysts
Zeolitas
Zeolites
Lantano
Lanthanum
Reacciones químicas
Chemical reactions
Hidrocarburos
Hydrocarbons
Craqueo
Cracking process
Hidrogenación
Hydrogenation
topic Catalizadores
Catalysts
Zeolitas
Zeolites
Lantano
Lanthanum
Reacciones químicas
Chemical reactions
Hidrocarburos
Hydrocarbons
Craqueo
Cracking process
Hidrogenación
Hydrogenation
description ABSTRACT: In the field of hydrocracking reactions, achieving optimal middle distillate yields remains a persistent challenge with commercially available zeolite Y catalysts. This limitation is attributed to challenges related to diffusion constraints within the catalyst. In response, we present a promising solution not only to these problems but also to the challenges encountered in nanosized Y zeolites when attempting to generate acidic sites within their structure and when analyzing their performance in vacuum gas oil hydrocracking. NiMo catalysts based on nanosized Y zeolites with different crystal sizes exchanged with lanthanum, effectively address diffusion issues and significantly enhance catalyst performance compared to dealuminated nanosized and commercial Y zeolite under the same reaction conditions. The catalysts were characterized by TGA, ICP-OES, XPS, N2 physisorption, FT-IR for pyridine acidity, TEM-mapping, and the 3-methyl thiophene reaction to test the hydrogenating capacity. Surface analysis and microscopy showed greater porosity in the catalysts with smaller zeolites and different arrangements of their components. The catalysts based on steamed protonated nanosized Y zeolites with a larger size and lanthanide nanosized Y zeolite with a smaller size yielded more middle distillates. Research provides a comprehensive analysis, providing a correlation between the catalytic performance and the size of the nanosized Y zeolite.
publishDate 2024
dc.date.issued.none.fl_str_mv 2024
dc.date.accessioned.none.fl_str_mv 2025-02-06T17:11:32Z
dc.date.available.none.fl_str_mv 2025-02-06T17:11:32Z
dc.type.spa.fl_str_mv Artículo de investigación
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dc.identifier.citation.spa.fl_str_mv Mendoza, Carlos & Manrique, Cecilia & Echavarria, Adriana. (2024). Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions. RSC Advances. 14. 26760-26774. 10.1039/d4ra04664a.
dc.identifier.uri.none.fl_str_mv https://hdl.handle.net/10495/44744
dc.identifier.doi.none.fl_str_mv 10.1039/d4ra04664a
dc.identifier.eissn.none.fl_str_mv 2046-2069
identifier_str_mv Mendoza, Carlos & Manrique, Cecilia & Echavarria, Adriana. (2024). Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions. RSC Advances. 14. 26760-26774. 10.1039/d4ra04664a.
10.1039/d4ra04664a
2046-2069
url https://hdl.handle.net/10495/44744
dc.language.iso.spa.fl_str_mv eng
language eng
dc.relation.ispartofjournalabbrev.spa.fl_str_mv RSC Adv.
dc.relation.citationendpage.spa.fl_str_mv 26774
dc.relation.citationissue.spa.fl_str_mv 37
dc.relation.citationstartpage.spa.fl_str_mv 26760
dc.relation.citationvolume.spa.fl_str_mv 14
dc.relation.ispartofjournal.spa.fl_str_mv RSC Advances
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dc.format.extent.spa.fl_str_mv 15 páginas
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dc.publisher.spa.fl_str_mv Royal Society of Chemistry
dc.publisher.place.spa.fl_str_mv Cambridge, Inglaterra
institution Universidad de Antioquia
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spelling Mendoza Merlano, Carlos JavierManrique Hernández, Alba CeciliaEchavarría Isaza, AdrianaCatalizadores y Adsorbentes2025-02-06T17:11:32Z2025-02-06T17:11:32Z2024Mendoza, Carlos & Manrique, Cecilia & Echavarria, Adriana. (2024). Impact of lanthanum ion exchange and steaming dealumination on middle distillate production using nanosized Y zeolite catalysts in hydrocracking reactions. RSC Advances. 14. 26760-26774. 10.1039/d4ra04664a.https://hdl.handle.net/10495/4474410.1039/d4ra04664a2046-2069ABSTRACT: In the field of hydrocracking reactions, achieving optimal middle distillate yields remains a persistent challenge with commercially available zeolite Y catalysts. This limitation is attributed to challenges related to diffusion constraints within the catalyst. In response, we present a promising solution not only to these problems but also to the challenges encountered in nanosized Y zeolites when attempting to generate acidic sites within their structure and when analyzing their performance in vacuum gas oil hydrocracking. NiMo catalysts based on nanosized Y zeolites with different crystal sizes exchanged with lanthanum, effectively address diffusion issues and significantly enhance catalyst performance compared to dealuminated nanosized and commercial Y zeolite under the same reaction conditions. The catalysts were characterized by TGA, ICP-OES, XPS, N2 physisorption, FT-IR for pyridine acidity, TEM-mapping, and the 3-methyl thiophene reaction to test the hydrogenating capacity. Surface analysis and microscopy showed greater porosity in the catalysts with smaller zeolites and different arrangements of their components. The catalysts based on steamed protonated nanosized Y zeolites with a larger size and lanthanide nanosized Y zeolite with a smaller size yielded more middle distillates. Research provides a comprehensive analysis, providing a correlation between the catalytic performance and the size of the nanosized Y zeolite.Universidad de Antioquia. Vicerrectoría de investigación. 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