Tri-potassium phosphate as a solid catalyst for biodiesel production from waste cooking oil
Transesterification of waste cooking oil with methanol, using tri-potassium phosphate as a solid catalyst, was investigated. Tri-potassium phosphate shows high catalytic properties for the transesterification reaction, compared to CaO and tri-sodium phosphate. Transesterification of waste cooking oi...
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Veröffentlicht in: | Fuel processing technology 2009-04, Vol.90 (4), p.520-524 |
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creator | Guan, Guoqing Kusakabe, Katsuki Yamasaki, Satoko |
description | Transesterification of waste cooking oil with methanol, using tri-potassium phosphate as a solid catalyst, was investigated. Tri-potassium phosphate shows high catalytic properties for the transesterification reaction, compared to CaO and tri-sodium phosphate. Transesterification of waste cooking oil required approximately two times more solid catalyst than transesterification of sunflower oil. The fatty acid methyl ester (FAME) yield reached 97.3% when the transesterification was performed with a catalyst concentration of 4 wt.% at 60 °C for 120 min. After regeneration of the used catalyst with aqueous KOH solution, the FAME yield recovered to 88%. Addition of a co-solvent changed the reaction state from three-phase to two-phase, but reduced the FAME yield, contrary to the results with homogeneous catalysts. The catalyst particles were easily agglomerated by the glycerol drops derived from the homogeneous liquid in the presence of co-solvents, reducing the catalytic activity. |
doi_str_mv | 10.1016/j.fuproc.2009.01.008 |
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Tri-potassium phosphate shows high catalytic properties for the transesterification reaction, compared to CaO and tri-sodium phosphate. Transesterification of waste cooking oil required approximately two times more solid catalyst than transesterification of sunflower oil. The fatty acid methyl ester (FAME) yield reached 97.3% when the transesterification was performed with a catalyst concentration of 4 wt.% at 60 °C for 120 min. After regeneration of the used catalyst with aqueous KOH solution, the FAME yield recovered to 88%. Addition of a co-solvent changed the reaction state from three-phase to two-phase, but reduced the FAME yield, contrary to the results with homogeneous catalysts. 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Tri-potassium phosphate shows high catalytic properties for the transesterification reaction, compared to CaO and tri-sodium phosphate. Transesterification of waste cooking oil required approximately two times more solid catalyst than transesterification of sunflower oil. The fatty acid methyl ester (FAME) yield reached 97.3% when the transesterification was performed with a catalyst concentration of 4 wt.% at 60 °C for 120 min. After regeneration of the used catalyst with aqueous KOH solution, the FAME yield recovered to 88%. Addition of a co-solvent changed the reaction state from three-phase to two-phase, but reduced the FAME yield, contrary to the results with homogeneous catalysts. The catalyst particles were easily agglomerated by the glycerol drops derived from the homogeneous liquid in the presence of co-solvents, reducing the catalytic activity.</description><subject>Applied sciences</subject><subject>Biodiesel</subject><subject>Biomass</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Natural energy</subject><subject>Solid catalyst</subject><subject>Tri-potassium phosphate</subject><issn>0378-3820</issn><issn>1873-7188</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2009</creationdate><recordtype>article</recordtype><recordid>eNp9ULtOwzAUtRBIlMcfMHiBLeHaDrW7ICHES0JigYnBcm5scEnj4JuA-HtSihiZznLejB0JKAWI-emyDGOfE5YSYFGCKAHMFpsJo1WhhTHbbAZKm0IZCbtsj2gJAGdnCz1jz485Fn0aHFEcV7x_TdS_usFzR9xxSm1sOLrBtV808JAyr2Nqoiff8imxGXGIqeMhpxX_dDTpMKW32L3wFNsDthNcS_7wF_fZ0_XV4-Vtcf9wc3d5cV9gpdRQVNK4MJ9LHdDLCuvayFobgdOIWi4WUkBTG3TzWhkEE0JovA5CVL4OugENap-dbHynRu-jp8GuIqFvW9f5NJJV1Xq4MBOx2hAxJ6Lsg-1zXLn8ZQXY9ZN2aTdP2vWTFoSdSkyy419_R-jakF2Hkf60Uihd6Z8e5xuen8Z-RJ8tYfQd-iZmj4NtUvw_6BtQG41Z</recordid><startdate>20090401</startdate><enddate>20090401</enddate><creator>Guan, Guoqing</creator><creator>Kusakabe, Katsuki</creator><creator>Yamasaki, Satoko</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>H8D</scope><scope>L7M</scope></search><sort><creationdate>20090401</creationdate><title>Tri-potassium phosphate as a solid catalyst for biodiesel production from waste cooking oil</title><author>Guan, Guoqing ; Kusakabe, Katsuki ; Yamasaki, Satoko</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c433t-428af6627fce24cbb82b781c008b299210db8ca6b38c08fffde7f114ebf7d0703</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2009</creationdate><topic>Applied sciences</topic><topic>Biodiesel</topic><topic>Biomass</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Natural energy</topic><topic>Solid catalyst</topic><topic>Tri-potassium phosphate</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Guan, Guoqing</creatorcontrib><creatorcontrib>Kusakabe, Katsuki</creatorcontrib><creatorcontrib>Yamasaki, Satoko</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Fuel processing technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Guan, Guoqing</au><au>Kusakabe, Katsuki</au><au>Yamasaki, Satoko</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Tri-potassium phosphate as a solid catalyst for biodiesel production from waste cooking oil</atitle><jtitle>Fuel processing technology</jtitle><date>2009-04-01</date><risdate>2009</risdate><volume>90</volume><issue>4</issue><spage>520</spage><epage>524</epage><pages>520-524</pages><issn>0378-3820</issn><eissn>1873-7188</eissn><coden>FPTEDY</coden><abstract>Transesterification of waste cooking oil with methanol, using tri-potassium phosphate as a solid catalyst, was investigated. Tri-potassium phosphate shows high catalytic properties for the transesterification reaction, compared to CaO and tri-sodium phosphate. Transesterification of waste cooking oil required approximately two times more solid catalyst than transesterification of sunflower oil. The fatty acid methyl ester (FAME) yield reached 97.3% when the transesterification was performed with a catalyst concentration of 4 wt.% at 60 °C for 120 min. After regeneration of the used catalyst with aqueous KOH solution, the FAME yield recovered to 88%. Addition of a co-solvent changed the reaction state from three-phase to two-phase, but reduced the FAME yield, contrary to the results with homogeneous catalysts. The catalyst particles were easily agglomerated by the glycerol drops derived from the homogeneous liquid in the presence of co-solvents, reducing the catalytic activity.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.fuproc.2009.01.008</doi><tpages>5</tpages></addata></record> |
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subjects | Applied sciences Biodiesel Biomass Energy Exact sciences and technology Natural energy Solid catalyst Tri-potassium phosphate |
title | Tri-potassium phosphate as a solid catalyst for biodiesel production from waste cooking oil |
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