Transesterification of waste cooking oil using Clay/CaO as a solid base catalyst

This study was conducted to investigate the use of clay/CaO heterogeneous catalyst for the production of biodiesel from waste cooking oil. The catalyst was synthesized from clay and calcined using calcium oxide under controlled conditions. Clay is a natural soil material containing a large amount of...

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Veröffentlicht in:Energy (Oxford) 2022-03, Vol.242, p.122536, Article 122536
Hauptverfasser: Mohadesi, Majid, Aghel, Babak, Gouran, Ashkan, Razmehgir, Mohammad Hamed
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Razmehgir, Mohammad Hamed
description This study was conducted to investigate the use of clay/CaO heterogeneous catalyst for the production of biodiesel from waste cooking oil. The catalyst was synthesized from clay and calcined using calcium oxide under controlled conditions. Clay is a natural soil material containing a large amount of amorphous silica. After processing calcium oxide and heating under controlled conditions at 800 °C, high surface area silica with amorphous structure was produced. The amorphous structure of the synthesized catalyst was confirmed by XRD analysis. The results of SEM analysis indicated that the particles had a spherical structure, distributed evenly and uniformly. The effect of five parameters of reaction temperature, catalyst concentration, oil to methanol volume ratio, toluene concentration, and reaction time on the purity of the biodiesel was evaluated through utilizing the response surface methodology (RSM). Under optimal conditions i.e. temperature of 54.97 °C, catalyst concentration of 9.6 wt%, oil to methanol volume ratio of 1.94 vol:vol, toluene concentration of 16.13 wt%, and reaction time of 74.32 min, the conversion rate was 97.16%. The results of catalyst recovery test showed that the prepared catalyst could be reused up to 5 times; thus, it can be used as a stable and cost-effective catalyst for the production of biodiesel. •Transesterification of waste cooking oil using CaO and Clay as catalysts was studied.•Clay/CaO catalyst characterized by XRF, SEM, FT-IR, and XRD.•The effect of operational parameters on biodiesel production was investigated.•Maximum FAME content of 97.16% has been obtained at the optimum condition.
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The catalyst was synthesized from clay and calcined using calcium oxide under controlled conditions. Clay is a natural soil material containing a large amount of amorphous silica. After processing calcium oxide and heating under controlled conditions at 800 °C, high surface area silica with amorphous structure was produced. The amorphous structure of the synthesized catalyst was confirmed by XRD analysis. The results of SEM analysis indicated that the particles had a spherical structure, distributed evenly and uniformly. The effect of five parameters of reaction temperature, catalyst concentration, oil to methanol volume ratio, toluene concentration, and reaction time on the purity of the biodiesel was evaluated through utilizing the response surface methodology (RSM). Under optimal conditions i.e. temperature of 54.97 °C, catalyst concentration of 9.6 wt%, oil to methanol volume ratio of 1.94 vol:vol, toluene concentration of 16.13 wt%, and reaction time of 74.32 min, the conversion rate was 97.16%. The results of catalyst recovery test showed that the prepared catalyst could be reused up to 5 times; thus, it can be used as a stable and cost-effective catalyst for the production of biodiesel. •Transesterification of waste cooking oil using CaO and Clay as catalysts was studied.•Clay/CaO catalyst characterized by XRF, SEM, FT-IR, and XRD.•The effect of operational parameters on biodiesel production was investigated.•Maximum FAME content of 97.16% has been obtained at the optimum condition.</description><identifier>ISSN: 0360-5442</identifier><identifier>EISSN: 1873-6785</identifier><identifier>DOI: 10.1016/j.energy.2021.122536</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Amorphous materials ; Amorphous structure ; Biodiesel ; Biodiesel fuels ; Biofuels ; Calcium ; Calcium oxide ; Catalysts ; Chemical synthesis ; Clay ; Clay soils ; Controlled conditions ; Cooking ; Cooking oils ; Diesel ; Lime ; Methanol ; Optimization ; Reaction time ; Response surface methodology ; Silica ; Silicon dioxide ; Toluene ; Transesterification ; Waste cooking oil</subject><ispartof>Energy (Oxford), 2022-03, Vol.242, p.122536, Article 122536</ispartof><rights>2021 Elsevier Ltd</rights><rights>Copyright Elsevier BV Mar 1, 2022</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c334t-af4307c640f597102d15a1624d2847981dd01f15271586e694ddb6f1049060193</citedby><cites>FETCH-LOGICAL-c334t-af4307c640f597102d15a1624d2847981dd01f15271586e694ddb6f1049060193</cites><orcidid>0000-0003-3584-5452 ; 0000-0003-1944-6435 ; 0000-0003-1939-8154</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.energy.2021.122536$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,777,781,3537,27905,27906,45976</link.rule.ids></links><search><creatorcontrib>Mohadesi, Majid</creatorcontrib><creatorcontrib>Aghel, Babak</creatorcontrib><creatorcontrib>Gouran, Ashkan</creatorcontrib><creatorcontrib>Razmehgir, Mohammad Hamed</creatorcontrib><title>Transesterification of waste cooking oil using Clay/CaO as a solid base catalyst</title><title>Energy (Oxford)</title><description>This study was conducted to investigate the use of clay/CaO heterogeneous catalyst for the production of biodiesel from waste cooking oil. 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subjects Amorphous materials
Amorphous structure
Biodiesel
Biodiesel fuels
Biofuels
Calcium
Calcium oxide
Catalysts
Chemical synthesis
Clay
Clay soils
Controlled conditions
Cooking
Cooking oils
Diesel
Lime
Methanol
Optimization
Reaction time
Response surface methodology
Silica
Silicon dioxide
Toluene
Transesterification
Waste cooking oil
title Transesterification of waste cooking oil using Clay/CaO as a solid base catalyst
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