A core-shell SO4/Mg-Al-Fe3O4 catalyst for biodiesel production

被引:111
作者
Gardy, Jabbar [1 ]
Nourafkan, Ehsan [2 ]
Osatiashtiani, Amin [3 ]
Lee, Adam F. [4 ]
Wilson, Karen [4 ]
Hassanpour, Ali [1 ]
Lai, Xiaojun [1 ]
机构
[1] Univ Leeds, Sch Chem & Proc Engn, Leeds LS2 9JT, W Yorkshire, England
[2] Univ Lincoln, Sch Math & Phys, Lincoln LN6 7TS, Lincs, England
[3] Aston Univ, European Bioenergy Res Inst, Birmingham B4 7ET, W Midlands, England
[4] RMIT Univ, Appl Chem & Environm Sci, Melbourne, Vic 3000, Australia
关键词
Solid acid catalyst; Magnetic catalyst; Core-shell nanoparticle; Waste cooking oil; Biodiesel; SOLID ACID CATALYST; OIL-BASED BIODIESEL; HETEROGENEOUS CATALYSIS; WASTE; ESTERIFICATION; SILICA; TIO2; NANOPARTICLES;
D O I
10.1016/j.apcatb.2019.118093
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Catalytic transesterification of triglycerides and esterification of free fatty acids underpins sustainable biodiesel production, wherein efficient heterogeneous catalysts are sought to replace mineral acids. A robust, magnetic core-shell SO4/Mg-Al-Fe3O4 catalyst was synthesised by stepwise co-precipitation, encapsulation, and surface functionalisation. The resulting magnetically-separable catalyst has a surface area of 123 m(2) g(-1), uniform 6.5 nm mesopores, and a high total acid site loading of 2.35 mmol g(-1). Optimum conditions for the (trans) esterification of waste cooking oil (WCO) over the sulfated solid acid catalyst were 95 degrees C, a methanol:WCO molar ratio of 9:1, and 300 min reaction to achieve 98.5% FAME yield. Esterification of oleic acid to methyl oleate resulted in an 88% yield after 150 min under the same reaction conditions. The magnetic solid acid catalyst exhibited good thermal and chemical stability and enabled facile catalyst separation post-reaction and the production of high quality biodiesel.
引用
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页数:10
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