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Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst

[Image: see text] The objective of this study was to prepare bifunctional catalysts based on iron and CaO and test them in the biodiesel production using waste cooking oil (WCO) as feedstock. Two iron precursors were studied, Fe(2)O(3) and Fe(NO(3))(3)·9H(2)O. The identified crystalline phases were...

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Autores principales: Enguilo Gonzaga, Vania, Romero, Rubi, Gómez-Espinosa, Rosa María, Romero, Amaya, Martínez, Sandra Luz, Natividad, Reyna
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2021
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8459442/
https://www.ncbi.nlm.nih.gov/pubmed/34568688
http://dx.doi.org/10.1021/acsomega.1c03586
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author Enguilo Gonzaga, Vania
Romero, Rubi
Gómez-Espinosa, Rosa María
Romero, Amaya
Martínez, Sandra Luz
Natividad, Reyna
author_facet Enguilo Gonzaga, Vania
Romero, Rubi
Gómez-Espinosa, Rosa María
Romero, Amaya
Martínez, Sandra Luz
Natividad, Reyna
author_sort Enguilo Gonzaga, Vania
collection PubMed
description [Image: see text] The objective of this study was to prepare bifunctional catalysts based on iron and CaO and test them in the biodiesel production using waste cooking oil (WCO) as feedstock. Two iron precursors were studied, Fe(2)O(3) and Fe(NO(3))(3)·9H(2)O. The identified crystalline phases were Ca(2)Fe(2)O(5) and CaFeO(3). Surface morphology and textural properties (distribution of active species, specific surface area, size, and pore volume) were also analyzed. Additionally, thermal stability was studied and 800 °C was established as the optimum calcination temperature. The density of both acidic and basic sites was higher with the catalyst prepared with Fe(2)O(3) than with that prepared with Fe(NO(3))(3)·9H(2)O. The latter, however, leads to reach equilibrium in half of the time than with the former. This was ascribed to the ratio of acidic to basic sites, which is higher with the catalyst prepared with the precursor salt. This ratio not only affects the overall cost of the process by affecting the time at which equilibrium is reached but also by dictating the methanol/oil molar ratio at which the equilibrium is reached sooner. The prepared bifunctional catalyst allowed us to produce biodiesel with 90% of methyl ester content at atmospheric pressure, reaction temperature of 60 °C, reaction time of 2 h, with 12:1 M ratio of methanol/WCO, 10 wt % of Fe over CaO, and a catalyst loading of 5 wt %. This catalyst can be used at least 3 times. The so-obtained biodiesel met the European norm EN-14214 regarding viscosity and density.
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spelling pubmed-84594422021-09-24 Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst Enguilo Gonzaga, Vania Romero, Rubi Gómez-Espinosa, Rosa María Romero, Amaya Martínez, Sandra Luz Natividad, Reyna ACS Omega [Image: see text] The objective of this study was to prepare bifunctional catalysts based on iron and CaO and test them in the biodiesel production using waste cooking oil (WCO) as feedstock. Two iron precursors were studied, Fe(2)O(3) and Fe(NO(3))(3)·9H(2)O. The identified crystalline phases were Ca(2)Fe(2)O(5) and CaFeO(3). Surface morphology and textural properties (distribution of active species, specific surface area, size, and pore volume) were also analyzed. Additionally, thermal stability was studied and 800 °C was established as the optimum calcination temperature. The density of both acidic and basic sites was higher with the catalyst prepared with Fe(2)O(3) than with that prepared with Fe(NO(3))(3)·9H(2)O. The latter, however, leads to reach equilibrium in half of the time than with the former. This was ascribed to the ratio of acidic to basic sites, which is higher with the catalyst prepared with the precursor salt. This ratio not only affects the overall cost of the process by affecting the time at which equilibrium is reached but also by dictating the methanol/oil molar ratio at which the equilibrium is reached sooner. The prepared bifunctional catalyst allowed us to produce biodiesel with 90% of methyl ester content at atmospheric pressure, reaction temperature of 60 °C, reaction time of 2 h, with 12:1 M ratio of methanol/WCO, 10 wt % of Fe over CaO, and a catalyst loading of 5 wt %. This catalyst can be used at least 3 times. The so-obtained biodiesel met the European norm EN-14214 regarding viscosity and density. American Chemical Society 2021-09-10 /pmc/articles/PMC8459442/ /pubmed/34568688 http://dx.doi.org/10.1021/acsomega.1c03586 Text en © 2021 The Authors. Published by American Chemical Society https://creativecommons.org/licenses/by-nc-nd/4.0/Permits non-commercial access and re-use, provided that author attribution and integrity are maintained; but does not permit creation of adaptations or other derivative works (https://creativecommons.org/licenses/by-nc-nd/4.0/).
spellingShingle Enguilo Gonzaga, Vania
Romero, Rubi
Gómez-Espinosa, Rosa María
Romero, Amaya
Martínez, Sandra Luz
Natividad, Reyna
Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst
title Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst
title_full Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst
title_fullStr Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst
title_full_unstemmed Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst
title_short Biodiesel Production from Waste Cooking Oil Catalyzed by a Bifunctional Catalyst
title_sort biodiesel production from waste cooking oil catalyzed by a bifunctional catalyst
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8459442/
https://www.ncbi.nlm.nih.gov/pubmed/34568688
http://dx.doi.org/10.1021/acsomega.1c03586
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