Chemical interesterification of soybean oil and methyl acetate to FAME using CaO as catalyst
•CaO as catalyst was assessed in interesterificaion reaction from soybean oil.•Catalyst was complete characterized and active in reaction.•Kinetic experiments allowed to evaluate the influence of main variables.•Ester content of 62.3 wt% was obtained in the best experimental condition.•Decreasing ca...
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Veröffentlicht in: | Fuel (Guildford) 2020-05, Vol.267, p.117264, Article 117264 |
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creator | Nunes, A.L.B. Castilhos, F. |
description | •CaO as catalyst was assessed in interesterificaion reaction from soybean oil.•Catalyst was complete characterized and active in reaction.•Kinetic experiments allowed to evaluate the influence of main variables.•Ester content of 62.3 wt% was obtained in the best experimental condition.•Decreasing catalytic activity was observed in reuse test.
This study evaluated calcium oxide as catalyst from calcium carbonate at different calcination temperatures and the hydration-dehydration technique was used to produce a nanocrystalline catalyst. CaO samples were characterized by XRD, thermogravimetric analysis, Fourier transform infrared spectroscopy, scanning electron microscopy and nitrogen adsorption/desorption. Interesterification reaction at 275 °C, 1: 40 M ratio (soybean oil: methyl acetate) and 6 wt% catalyst concentration for 120 min was used with Tukey's test to determine the best calcination temperature, 800 °C. Selected catalyst was used in kinetic experiments to evaluate the effect of temperature, catalyst concentration and Oil:MeA molar ratio. The optimum condition was 325 °C, catalyst content of 10 wt%, and 1:40 Oil:MeA molar ratio, with a 62.3 wt% FAME content. Reuse catalyst was tested and the results showed a decreasing catalytic activity. Leaching test and FTIR analyses of the catalyst pointed out to mass loss and adsorbents at the basic sites would be contributing to CaO deactivation. |
doi_str_mv | 10.1016/j.fuel.2020.117264 |
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This study evaluated calcium oxide as catalyst from calcium carbonate at different calcination temperatures and the hydration-dehydration technique was used to produce a nanocrystalline catalyst. CaO samples were characterized by XRD, thermogravimetric analysis, Fourier transform infrared spectroscopy, scanning electron microscopy and nitrogen adsorption/desorption. Interesterification reaction at 275 °C, 1: 40 M ratio (soybean oil: methyl acetate) and 6 wt% catalyst concentration for 120 min was used with Tukey's test to determine the best calcination temperature, 800 °C. Selected catalyst was used in kinetic experiments to evaluate the effect of temperature, catalyst concentration and Oil:MeA molar ratio. The optimum condition was 325 °C, catalyst content of 10 wt%, and 1:40 Oil:MeA molar ratio, with a 62.3 wt% FAME content. Reuse catalyst was tested and the results showed a decreasing catalytic activity. Leaching test and FTIR analyses of the catalyst pointed out to mass loss and adsorbents at the basic sites would be contributing to CaO deactivation.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2020.117264</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Acetic acid ; Calcium ; Calcium carbonate ; Calcium oxide ; Catalysts ; Catalytic activity ; Deactivation ; Dehydration ; Fourier analysis ; Fourier transforms ; Heterogeneous catalysis ; Infrared analysis ; Infrared spectroscopy ; Kinetics ; Leaching ; Lime ; Methyl acetate ; Methyl ester ; Roasting ; Scanning electron microscopy ; Soybean oil ; Soybeans ; Temperature effects ; Thermogravimetric analysis ; Triacetin</subject><ispartof>Fuel (Guildford), 2020-05, Vol.267, p.117264, Article 117264</ispartof><rights>2020 Elsevier Ltd</rights><rights>Copyright Elsevier BV May 1, 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c328t-24155d6095d84f37985c01d742e736468e62b73485e7eafd51d25e1a013db4403</citedby><cites>FETCH-LOGICAL-c328t-24155d6095d84f37985c01d742e736468e62b73485e7eafd51d25e1a013db4403</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0016236120302593$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids></links><search><creatorcontrib>Nunes, A.L.B.</creatorcontrib><creatorcontrib>Castilhos, F.</creatorcontrib><title>Chemical interesterification of soybean oil and methyl acetate to FAME using CaO as catalyst</title><title>Fuel (Guildford)</title><description>•CaO as catalyst was assessed in interesterificaion reaction from soybean oil.•Catalyst was complete characterized and active in reaction.•Kinetic experiments allowed to evaluate the influence of main variables.•Ester content of 62.3 wt% was obtained in the best experimental condition.•Decreasing catalytic activity was observed in reuse test.
This study evaluated calcium oxide as catalyst from calcium carbonate at different calcination temperatures and the hydration-dehydration technique was used to produce a nanocrystalline catalyst. CaO samples were characterized by XRD, thermogravimetric analysis, Fourier transform infrared spectroscopy, scanning electron microscopy and nitrogen adsorption/desorption. Interesterification reaction at 275 °C, 1: 40 M ratio (soybean oil: methyl acetate) and 6 wt% catalyst concentration for 120 min was used with Tukey's test to determine the best calcination temperature, 800 °C. Selected catalyst was used in kinetic experiments to evaluate the effect of temperature, catalyst concentration and Oil:MeA molar ratio. The optimum condition was 325 °C, catalyst content of 10 wt%, and 1:40 Oil:MeA molar ratio, with a 62.3 wt% FAME content. Reuse catalyst was tested and the results showed a decreasing catalytic activity. Leaching test and FTIR analyses of the catalyst pointed out to mass loss and adsorbents at the basic sites would be contributing to CaO deactivation.</description><subject>Acetic acid</subject><subject>Calcium</subject><subject>Calcium carbonate</subject><subject>Calcium oxide</subject><subject>Catalysts</subject><subject>Catalytic activity</subject><subject>Deactivation</subject><subject>Dehydration</subject><subject>Fourier analysis</subject><subject>Fourier transforms</subject><subject>Heterogeneous catalysis</subject><subject>Infrared analysis</subject><subject>Infrared spectroscopy</subject><subject>Kinetics</subject><subject>Leaching</subject><subject>Lime</subject><subject>Methyl acetate</subject><subject>Methyl ester</subject><subject>Roasting</subject><subject>Scanning electron microscopy</subject><subject>Soybean oil</subject><subject>Soybeans</subject><subject>Temperature effects</subject><subject>Thermogravimetric analysis</subject><subject>Triacetin</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9UE1Lw0AUXETBWv0DnhY8p-5nNgUvJbQqVHrRm7Bssy92Q5rU3Y2Qf--WePby3jDMvI9B6J6SBSU0f2wW9QDtghGWCKpYLi7QjBaKZ4pKfolmJKkyxnN6jW5CaAghqpBihj7LAxxdZVrsuggeQiquTkR0fYf7God-3INJ0LXYdBYfIR7GBCuIJgKOPd6s3tZ4CK77wqXZYRNwcpt2DPEWXdWmDXD31-foY7N-L1-y7e75tVxts4qzImZMUCltTpbSFqLmalnIilCrBAPFc5EXkLO94qKQoMDUVlLLJFBDKLd7IQifo4dp7sn330P6QTf94Lu0UjPBCkqUksukYpOq8n0IHmp98u5o_Kgp0ecUdaPPKepzinpKMZmeJhOk-38ceB0qB10F1nmoora9-8_-C87-eXY</recordid><startdate>20200501</startdate><enddate>20200501</enddate><creator>Nunes, A.L.B.</creator><creator>Castilhos, F.</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope></search><sort><creationdate>20200501</creationdate><title>Chemical interesterification of soybean oil and methyl acetate to FAME using CaO as catalyst</title><author>Nunes, A.L.B. ; Castilhos, F.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c328t-24155d6095d84f37985c01d742e736468e62b73485e7eafd51d25e1a013db4403</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Acetic acid</topic><topic>Calcium</topic><topic>Calcium carbonate</topic><topic>Calcium oxide</topic><topic>Catalysts</topic><topic>Catalytic activity</topic><topic>Deactivation</topic><topic>Dehydration</topic><topic>Fourier analysis</topic><topic>Fourier transforms</topic><topic>Heterogeneous catalysis</topic><topic>Infrared analysis</topic><topic>Infrared spectroscopy</topic><topic>Kinetics</topic><topic>Leaching</topic><topic>Lime</topic><topic>Methyl acetate</topic><topic>Methyl ester</topic><topic>Roasting</topic><topic>Scanning electron microscopy</topic><topic>Soybean oil</topic><topic>Soybeans</topic><topic>Temperature effects</topic><topic>Thermogravimetric analysis</topic><topic>Triacetin</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Nunes, A.L.B.</creatorcontrib><creatorcontrib>Castilhos, F.</creatorcontrib><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><jtitle>Fuel (Guildford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Nunes, A.L.B.</au><au>Castilhos, F.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Chemical interesterification of soybean oil and methyl acetate to FAME using CaO as catalyst</atitle><jtitle>Fuel (Guildford)</jtitle><date>2020-05-01</date><risdate>2020</risdate><volume>267</volume><spage>117264</spage><pages>117264-</pages><artnum>117264</artnum><issn>0016-2361</issn><eissn>1873-7153</eissn><abstract>•CaO as catalyst was assessed in interesterificaion reaction from soybean oil.•Catalyst was complete characterized and active in reaction.•Kinetic experiments allowed to evaluate the influence of main variables.•Ester content of 62.3 wt% was obtained in the best experimental condition.•Decreasing catalytic activity was observed in reuse test.
This study evaluated calcium oxide as catalyst from calcium carbonate at different calcination temperatures and the hydration-dehydration technique was used to produce a nanocrystalline catalyst. CaO samples were characterized by XRD, thermogravimetric analysis, Fourier transform infrared spectroscopy, scanning electron microscopy and nitrogen adsorption/desorption. Interesterification reaction at 275 °C, 1: 40 M ratio (soybean oil: methyl acetate) and 6 wt% catalyst concentration for 120 min was used with Tukey's test to determine the best calcination temperature, 800 °C. Selected catalyst was used in kinetic experiments to evaluate the effect of temperature, catalyst concentration and Oil:MeA molar ratio. The optimum condition was 325 °C, catalyst content of 10 wt%, and 1:40 Oil:MeA molar ratio, with a 62.3 wt% FAME content. Reuse catalyst was tested and the results showed a decreasing catalytic activity. Leaching test and FTIR analyses of the catalyst pointed out to mass loss and adsorbents at the basic sites would be contributing to CaO deactivation.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2020.117264</doi></addata></record> |
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subjects | Acetic acid Calcium Calcium carbonate Calcium oxide Catalysts Catalytic activity Deactivation Dehydration Fourier analysis Fourier transforms Heterogeneous catalysis Infrared analysis Infrared spectroscopy Kinetics Leaching Lime Methyl acetate Methyl ester Roasting Scanning electron microscopy Soybean oil Soybeans Temperature effects Thermogravimetric analysis Triacetin |
title | Chemical interesterification of soybean oil and methyl acetate to FAME using CaO as catalyst |
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