Upgrading of coal liquids by Hydrous Metal Oxide catalysts

Hydrous Metal Oxides (HMOs) are chemically synthesized materials which contain a homogeneous distribution of ion exchangeable alkali cations that provide charge compensation to the metal-oxygen framework. Both the presence of these alkali cations and the resulting high cation exchange capacities (4-...

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Váldodahkkit: Sandia National Labs., Albuquerque, NM (United States), S Lott, USDOE, Washington, DC (United States), T Gardner, L McLaughlin, J.B. Oelfke
Materiálatiipa: Report
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Almmustuhtton: 1994
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Liŋkkat:https://www.osti.gov/servlets/purl/10158468
https://doi.org/10.2172/10176929
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author Sandia National Labs., Albuquerque, NM (United States)
S Lott
USDOE, Washington, DC (United States)
T Gardner
L McLaughlin
J.B. Oelfke
author_browse J.B. Oelfke
L McLaughlin
S Lott
Sandia National Labs., Albuquerque, NM (United States)
T Gardner
USDOE, Washington, DC (United States)
author_facet Sandia National Labs., Albuquerque, NM (United States)
S Lott
USDOE, Washington, DC (United States)
T Gardner
L McLaughlin
J.B. Oelfke
author_sort Sandia National Labs., Albuquerque, NM (United States)
collection OpenAlex (Petróleo y Energía)
description Hydrous Metal Oxides (HMOs) are chemically synthesized materials which contain a homogeneous distribution of ion exchangeable alkali cations that provide charge compensation to the metal-oxygen framework. Both the presence of these alkali cations and the resulting high cation exchange capacities (4--5 meq/g) clearly set these HMO materials apart from conventional precipitated hydrous oxides. For catalyst applications, the HMO material serves as an ion exchangeable support which facilitates the uniform incorporation of catalyst precursor species. Following catalyst precursor incorporation, an activation step is required to convert the catalyst precursor to the desired active phase. Considerable process development activities at Sandia National Laboratories related to HMO materials have resulted in bulk silica-doped hydrous titanium oxide (HTO:Si)-supported NiMo catalysts that are more active in model compound reactions than commercial NiMo catalysts. These reactions, e.g. pyrene hydrogenation, simulate direct coal liquefaction. However, extension of this process to produce NiMo/HTO:Si catalyst coatings on commercial supports is of interest for liquefaction applications since overall catalyst cost can be reduced and bulk HTO:SI mechanical limitations can be circumvented. In the present effort, NiMo/HTO:Si has been evaluated for hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) of coal derived liquids. NiMo/HTO:Si catalysts have been evaluated in both bulk (unsupported) form and a supported form on commercial alumina extrudates.
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spelling Upgrading of coal liquids by Hydrous Metal Oxide catalysts Sandia National Labs., Albuquerque, NM (United States) S Lott USDOE, Washington, DC (United States) T Gardner L McLaughlin J.B. Oelfke Catalysis and Hydrodesulfurization Studies Nanomaterials for catalytic reactions Petroleum Processing and Analysis hydrous metal oxides NiMo catalysts coal liquefaction coal liquids hydrodesulfurization hydrodenitrogenation supported catalysts cation exchange capacity Hydrous Metal Oxides (HMOs) are chemically synthesized materials which contain a homogeneous distribution of ion exchangeable alkali cations that provide charge compensation to the metal-oxygen framework. Both the presence of these alkali cations and the resulting high cation exchange capacities (4--5 meq/g) clearly set these HMO materials apart from conventional precipitated hydrous oxides. For catalyst applications, the HMO material serves as an ion exchangeable support which facilitates the uniform incorporation of catalyst precursor species. Following catalyst precursor incorporation, an activation step is required to convert the catalyst precursor to the desired active phase. Considerable process development activities at Sandia National Laboratories related to HMO materials have resulted in bulk silica-doped hydrous titanium oxide (HTO:Si)-supported NiMo catalysts that are more active in model compound reactions than commercial NiMo catalysts. These reactions, e.g. pyrene hydrogenation, simulate direct coal liquefaction. However, extension of this process to produce NiMo/HTO:Si catalyst coatings on commercial supports is of interest for liquefaction applications since overall catalyst cost can be reduced and bulk HTO:SI mechanical limitations can be circumvented. In the present effort, NiMo/HTO:Si has been evaluated for hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) of coal derived liquids. NiMo/HTO:Si catalysts have been evaluated in both bulk (unsupported) form and a supported form on commercial alumina extrudates.
spellingShingle Upgrading of coal liquids by Hydrous Metal Oxide catalysts
Sandia National Labs., Albuquerque, NM (United States)
S Lott
USDOE, Washington, DC (United States)
T Gardner
L McLaughlin
J.B. Oelfke
Catalysis and Hydrodesulfurization Studies
Nanomaterials for catalytic reactions
Petroleum Processing and Analysis
hydrous metal oxides
NiMo catalysts
coal liquefaction
coal liquids
hydrodesulfurization
hydrodenitrogenation
supported catalysts
cation exchange capacity
title Upgrading of coal liquids by Hydrous Metal Oxide catalysts
title_full Upgrading of coal liquids by Hydrous Metal Oxide catalysts
title_fullStr Upgrading of coal liquids by Hydrous Metal Oxide catalysts
title_full_unstemmed Upgrading of coal liquids by Hydrous Metal Oxide catalysts
title_short Upgrading of coal liquids by Hydrous Metal Oxide catalysts
topic Catalysis and Hydrodesulfurization Studies
Nanomaterials for catalytic reactions
Petroleum Processing and Analysis
hydrous metal oxides
NiMo catalysts
coal liquefaction
coal liquids
hydrodesulfurization
hydrodenitrogenation
supported catalysts
cation exchange capacity
topic_facet Catalysis and Hydrodesulfurization Studies
Nanomaterials for catalytic reactions
Petroleum Processing and Analysis
hydrous metal oxides
NiMo catalysts
coal liquefaction
coal liquids
hydrodesulfurization
hydrodenitrogenation
supported catalysts
cation exchange capacity
url https://www.osti.gov/servlets/purl/10158468
https://doi.org/10.2172/10176929