Roles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading

Light cycle oil (LCO) is one of the major products in Fluid catalytic cracking (FCC) processes, and has drawbacks such as high aromatics, sulfur, and nitrogen contents, and low cetane number (CN). Hydro-upgrading is one of the most typical processes for LCO upgrading, and alumina-zeolite (AZ) is an...

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Autores principales: Jianglong Pu, Haiping Zhang, Min Wang, Kyle Rogers, Hongmei Wang, Hui Wang, Siauw Ng, Ping Sun
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Publicado: MDPI AG 2021
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Acceso en línea:https://doaj.org/article/6c47b499eea54390a2b2d59fb2d1b033
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spelling oai:doaj.org-article:6c47b499eea54390a2b2d59fb2d1b0332021-11-25T17:05:22ZRoles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading10.3390/catal111112772073-4344https://doaj.org/article/6c47b499eea54390a2b2d59fb2d1b0332021-10-01T00:00:00Zhttps://www.mdpi.com/2073-4344/11/11/1277https://doaj.org/toc/2073-4344Light cycle oil (LCO) is one of the major products in Fluid catalytic cracking (FCC) processes, and has drawbacks such as high aromatics, sulfur, and nitrogen contents, and low cetane number (CN). Hydro-upgrading is one of the most typical processes for LCO upgrading, and alumina-zeolite (AZ) is an effective hydrotreating catalyst support. This paper examined the effects of different bimetallic catalysts (CoMo/AZ, NiMo/AZ, and NiW/AZ) supported by AZ on hydro-upgrading of both model compounds and real LCO. CoMo/AZ preferred the direct desulfurization (DDS) route while the NiMo/AZ and NiW/AZ catalysts favored the desulfurization route through hydrogenation (HYD). The presence of nitrogen compounds in the feed introduced a competitive adsorption mechanism and reduced the number of available acid sites. Aromatics were partially hydrogenated into methyltetralines at first, and then further hydrogenated, cracked, and isomerized into methyldecalins, monocyclic, and methyltetralines isomers. CoMo/AZ is the best hydrodesulfurization (HDS) catalyst for the model compounds at low H<sub>2</sub> pressure (550 psi) and for LCO at lower temperature (573 K), while NiMo/AZ performs the best for LCO at higher temperature (648 K). NiMo/AZ is the best hydrodenitrogenation (HDN) catalyst for LCO. The hydrodearomatization (HDA) performances of NiMo/AZ and NiW/AZ improved significantly and overwhelmingly higher than that of the CoMo/AZ when the H<sub>2</sub> pressure was increased to 1100 psi.Jianglong PuHaiping ZhangMin WangKyle RogersHongmei WangHui WangSiauw NgPing SunMDPI AGarticlebimetallicalumina-zeolite supportlight cycle oilhydrodesulfurizationhydrodenitrogenationhydrodearomatizationChemical technologyTP1-1185ChemistryQD1-999ENCatalysts, Vol 11, Iss 1277, p 1277 (2021)
institution DOAJ
collection DOAJ
language EN
topic bimetallic
alumina-zeolite support
light cycle oil
hydrodesulfurization
hydrodenitrogenation
hydrodearomatization
Chemical technology
TP1-1185
Chemistry
QD1-999
spellingShingle bimetallic
alumina-zeolite support
light cycle oil
hydrodesulfurization
hydrodenitrogenation
hydrodearomatization
Chemical technology
TP1-1185
Chemistry
QD1-999
Jianglong Pu
Haiping Zhang
Min Wang
Kyle Rogers
Hongmei Wang
Hui Wang
Siauw Ng
Ping Sun
Roles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading
description Light cycle oil (LCO) is one of the major products in Fluid catalytic cracking (FCC) processes, and has drawbacks such as high aromatics, sulfur, and nitrogen contents, and low cetane number (CN). Hydro-upgrading is one of the most typical processes for LCO upgrading, and alumina-zeolite (AZ) is an effective hydrotreating catalyst support. This paper examined the effects of different bimetallic catalysts (CoMo/AZ, NiMo/AZ, and NiW/AZ) supported by AZ on hydro-upgrading of both model compounds and real LCO. CoMo/AZ preferred the direct desulfurization (DDS) route while the NiMo/AZ and NiW/AZ catalysts favored the desulfurization route through hydrogenation (HYD). The presence of nitrogen compounds in the feed introduced a competitive adsorption mechanism and reduced the number of available acid sites. Aromatics were partially hydrogenated into methyltetralines at first, and then further hydrogenated, cracked, and isomerized into methyldecalins, monocyclic, and methyltetralines isomers. CoMo/AZ is the best hydrodesulfurization (HDS) catalyst for the model compounds at low H<sub>2</sub> pressure (550 psi) and for LCO at lower temperature (573 K), while NiMo/AZ performs the best for LCO at higher temperature (648 K). NiMo/AZ is the best hydrodenitrogenation (HDN) catalyst for LCO. The hydrodearomatization (HDA) performances of NiMo/AZ and NiW/AZ improved significantly and overwhelmingly higher than that of the CoMo/AZ when the H<sub>2</sub> pressure was increased to 1100 psi.
format article
author Jianglong Pu
Haiping Zhang
Min Wang
Kyle Rogers
Hongmei Wang
Hui Wang
Siauw Ng
Ping Sun
author_facet Jianglong Pu
Haiping Zhang
Min Wang
Kyle Rogers
Hongmei Wang
Hui Wang
Siauw Ng
Ping Sun
author_sort Jianglong Pu
title Roles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading
title_short Roles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading
title_full Roles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading
title_fullStr Roles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading
title_full_unstemmed Roles of Nanostructured Bimetallic Supported on Alumina-Zeolite (AZ) in Light Cycle Oil (LCO) Upgrading
title_sort roles of nanostructured bimetallic supported on alumina-zeolite (az) in light cycle oil (lco) upgrading
publisher MDPI AG
publishDate 2021
url https://doaj.org/article/6c47b499eea54390a2b2d59fb2d1b033
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