Article ID Journal Published Year Pages File Type
40533 Applied Catalysis A: General 2013 6 Pages PDF
Abstract

Biodiesel production by simultaneous esterification and transesterification of waste oil with methanol has been studied in a heterogeneous system using solid ferric hydrogen sulphate [Fe (HSO4)3] acid catalyst. The catalyst was prepared by displacement reaction followed by calcination at 400 °C for 3 h. The prepared catalyst was characterized using X-ray diffraction (XRD), Fourier transform infrared spectrometer (FT-IR), Brunner-Emmett-Teller surface area measurement (BET), thermal gravimetric analyzer (TGA) and temperature-programmed desorption of NH3 (TPD - NH3). Furthermore, the dependence of the conversion of mixed waste oil on the reactions variables such as the molar ratio of methanol/oil, the amount of catalysts used, reaction temperatures, reusability were also investigated. The catalyst was reused many times with slight loss in activity and the maximum yield of 94.5% was achieved at the optimized conditions of reaction temperature of 205 °C; stirring speed of 350 rpm, 1:15 molar ratio of oil to alcohol and 1% w/w catalyst loading.

Graphical abstractFigure optionsDownload full-size imageDownload high-quality image (42 K)Download as PowerPoint slideHighlights► The catalyst was prepared through replacement reaction (sulfation). ► The high activity of the catalyst was described to strong acidity. ► Fe (HSO4)3 is able to convert simultaneously TAG and FFA in FAMEs with high yield. ► The maximum yield was achieved as 94.5% at optimized condition. ► It is possible to convert oils with very high FFAs content into FAMEs.

Related Topics
Physical Sciences and Engineering Chemical Engineering Catalysis
Authors
, , , , , , ,