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Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel

The effect of the sulfur and metal-type content of MoP-S/γ-Al(2)O(3)-MgO, NiMoP-S/γ-Al(2)O(3)-MgO, and NiP-S/γ-Al(2)O(3)-MgO phosphide on hydroprocessing (HDO, HDCx-HDCn, HCK, HYD, and HYG) of fatty acids was studied. The catalysts were characterized by XRF, XRD, textural properties, XPS, Raman, Py-...

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Autores principales: Puello-Polo, Esneyder, Arias, Dana, Márquez, Edgar
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Frontiers Media S.A. 2022
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9125250/
https://www.ncbi.nlm.nih.gov/pubmed/35615310
http://dx.doi.org/10.3389/fchem.2022.880051
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author Puello-Polo, Esneyder
Arias, Dana
Márquez, Edgar
author_facet Puello-Polo, Esneyder
Arias, Dana
Márquez, Edgar
author_sort Puello-Polo, Esneyder
collection PubMed
description The effect of the sulfur and metal-type content of MoP-S/γ-Al(2)O(3)-MgO, NiMoP-S/γ-Al(2)O(3)-MgO, and NiP-S/γ-Al(2)O(3)-MgO phosphide on hydroprocessing (HDO, HDCx-HDCn, HCK, HYD, and HYG) of fatty acids was studied. The catalysts were characterized by XRF, XRD, textural properties, XPS, Raman, Py-TPD, and EDS elemental mapping. The chemical analyses by X-ray fluorescence (XRF), EDS elemental mapping, and CHNS-O elemental analysis showed stoichiometric values Al/Mg = 38–40, Mo:Ni:P ∼ 1, and S ≤ 4.5 wt % (this value means that the molar ratio Mo:S ∼ 1.0:1.6, i.e., MoS(2)); also EDS elemental mapping confirmed the presence of Mo, Ni, Al, O, P, Mg, and S with good distribution on Al(2)O(3)-MgO. The impregnation of metals leads to a decrease in the surface area and pore volume as follows NiMoP-S/γ-Al(2)O(3)-MgO < MoP-S/γ-Al(2)O(3)-MgO < NiP-S/γ-Al(2)O(3)-MgO < Al(2)O(3)-MgO < Al(2)O(3) (unimodal pore size distribution), propitiating a pseudo bimodal pore size distribution with Dp-BJH between ∼5–7 nm and 11.8–14.2 nm for the presence of MgO. XRD confirmed differences between metallic phosphates and phosphides, and XPS confirmed the presence at the surface of Mo(δ+)(0 < δ+ < 2), Mo(4+), Mo(6+), Ni(δ+)(0 < δ+ < 2), Ni(2+), S(2−), SO(4) (2−), P(δ+), and P(5+) species. Raman revealed the presence of MoS(2) only in MoP-S/γ-Al(2)O(3)-MgO and NiMoP-S/γ-Al(2)O(3)-MgO, while the NiMoP-S/γ-Al(2)O(3)-MgO catalyst had a more significant number of Brønsted and Lewis sites, although the increasing temperature decreased the Lewis sites. MoP-S/γ-Al(2)O(3)-MgO was more active at HDO showing the highest production rate for octadecane of 53 mol/(g(cat)·h), whereas NiP-S/γ-Al(2)O(3)-MgO was more active at HDCx-HDCn [45 mol/(g(cat)·h)] and HCK [6 mol/(g(cat)·h)]; meanwhile, NiMoP-S/γ-Al(2)O(3)-MgO had a mix of HDO [47 mol/(g(cat)·h)] and HDCx-HDCn [41 mol/(g(cat)·h)]. This showed production towards octadecane, heptadecane, and light hydrocarbons, meaning that the fatty acids were deoxygenated through bifunctional sites for hydrogenation (HYD) and hydrogenolysis (HYG) as follows: MoP-S/γ-Al(2)O(3)-MgO (K(1) = 0.08 and K(2) = 0.03 L/mol) < NiMoP-S/γ-Al(2)O(3)-MgO (K(1) = 0.25 and K(2) = 0.45 L/mol) < NiP-S/γ-Al(2)O(3)-MgO (K(1) = 2.5 and K(2) = 6.5 L/mol). For this reason, we considered that phosphide acts as a structural promoter with sulfur on its surface as a “mixed phosphidic-sulphidic species”, allowing the largest generation of heptadecane and octadecane by the presence of BRIM sites for HYD and CUS sites for HYG.
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spelling pubmed-91252502022-05-24 Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel Puello-Polo, Esneyder Arias, Dana Márquez, Edgar Front Chem Chemistry The effect of the sulfur and metal-type content of MoP-S/γ-Al(2)O(3)-MgO, NiMoP-S/γ-Al(2)O(3)-MgO, and NiP-S/γ-Al(2)O(3)-MgO phosphide on hydroprocessing (HDO, HDCx-HDCn, HCK, HYD, and HYG) of fatty acids was studied. The catalysts were characterized by XRF, XRD, textural properties, XPS, Raman, Py-TPD, and EDS elemental mapping. The chemical analyses by X-ray fluorescence (XRF), EDS elemental mapping, and CHNS-O elemental analysis showed stoichiometric values Al/Mg = 38–40, Mo:Ni:P ∼ 1, and S ≤ 4.5 wt % (this value means that the molar ratio Mo:S ∼ 1.0:1.6, i.e., MoS(2)); also EDS elemental mapping confirmed the presence of Mo, Ni, Al, O, P, Mg, and S with good distribution on Al(2)O(3)-MgO. The impregnation of metals leads to a decrease in the surface area and pore volume as follows NiMoP-S/γ-Al(2)O(3)-MgO < MoP-S/γ-Al(2)O(3)-MgO < NiP-S/γ-Al(2)O(3)-MgO < Al(2)O(3)-MgO < Al(2)O(3) (unimodal pore size distribution), propitiating a pseudo bimodal pore size distribution with Dp-BJH between ∼5–7 nm and 11.8–14.2 nm for the presence of MgO. XRD confirmed differences between metallic phosphates and phosphides, and XPS confirmed the presence at the surface of Mo(δ+)(0 < δ+ < 2), Mo(4+), Mo(6+), Ni(δ+)(0 < δ+ < 2), Ni(2+), S(2−), SO(4) (2−), P(δ+), and P(5+) species. Raman revealed the presence of MoS(2) only in MoP-S/γ-Al(2)O(3)-MgO and NiMoP-S/γ-Al(2)O(3)-MgO, while the NiMoP-S/γ-Al(2)O(3)-MgO catalyst had a more significant number of Brønsted and Lewis sites, although the increasing temperature decreased the Lewis sites. MoP-S/γ-Al(2)O(3)-MgO was more active at HDO showing the highest production rate for octadecane of 53 mol/(g(cat)·h), whereas NiP-S/γ-Al(2)O(3)-MgO was more active at HDCx-HDCn [45 mol/(g(cat)·h)] and HCK [6 mol/(g(cat)·h)]; meanwhile, NiMoP-S/γ-Al(2)O(3)-MgO had a mix of HDO [47 mol/(g(cat)·h)] and HDCx-HDCn [41 mol/(g(cat)·h)]. This showed production towards octadecane, heptadecane, and light hydrocarbons, meaning that the fatty acids were deoxygenated through bifunctional sites for hydrogenation (HYD) and hydrogenolysis (HYG) as follows: MoP-S/γ-Al(2)O(3)-MgO (K(1) = 0.08 and K(2) = 0.03 L/mol) < NiMoP-S/γ-Al(2)O(3)-MgO (K(1) = 0.25 and K(2) = 0.45 L/mol) < NiP-S/γ-Al(2)O(3)-MgO (K(1) = 2.5 and K(2) = 6.5 L/mol). For this reason, we considered that phosphide acts as a structural promoter with sulfur on its surface as a “mixed phosphidic-sulphidic species”, allowing the largest generation of heptadecane and octadecane by the presence of BRIM sites for HYD and CUS sites for HYG. Frontiers Media S.A. 2022-05-09 /pmc/articles/PMC9125250/ /pubmed/35615310 http://dx.doi.org/10.3389/fchem.2022.880051 Text en Copyright © 2022 Puello-Polo, Arias and Márquez. https://creativecommons.org/licenses/by/4.0/This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.
spellingShingle Chemistry
Puello-Polo, Esneyder
Arias, Dana
Márquez, Edgar
Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel
title Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel
title_full Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel
title_fullStr Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel
title_full_unstemmed Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel
title_short Al(2)O(3)-MgO Supported Ni, Mo, and NiMo Mixed Phosphidic-Sulphidic Phase for Hydrotreating of Stearic and Oleic Acids Into Green Diesel
title_sort al(2)o(3)-mgo supported ni, mo, and nimo mixed phosphidic-sulphidic phase for hydrotreating of stearic and oleic acids into green diesel
topic Chemistry
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9125250/
https://www.ncbi.nlm.nih.gov/pubmed/35615310
http://dx.doi.org/10.3389/fchem.2022.880051
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