Production of biodiesel from mixed waste vegetable oils using Ferric hydrogen sulphate as an effective reusable heterogeneous solid acid catalyst

被引:74
|
作者
Alhassan, Fatah H. [1 ,2 ]
Yunus, Robiah [3 ]
Rashid, Umer [3 ]
Sirat, Kamaliah [2 ]
Islam, Aminul [1 ,2 ]
Lee, H. V. [1 ,2 ]
Taufiq-Yap, Yun H. [1 ,2 ]
机构
[1] Univ Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Upm Serdang 43400, Selangor, Malaysia
[2] Univ Putra Malaysia, Fac Sci, Dept Chem, Upm Serdang 43400, Selangor, Malaysia
[3] Univ Putra Malaysia, Inst Adv Technol, Upm Serdang 43400, Selangor, Malaysia
关键词
Biodiesel; Ferric hydrogen sulphate; Esterification; Transesterification; Mixed waste vegetable oil; Reusable; FREE FATTY-ACIDS; SUNFLOWER OIL; SOYBEAN OIL; TRANSESTERIFICATION; OPTIMIZATION; ZEOLITES; ZIRCONIA; PALM;
D O I
10.1016/j.apcata.2013.02.019
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
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 degrees 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 degrees C; stirring speed of 350 rpm, 1:15 molar ratio of oil to alcohol and 1% w/w catalyst loading. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:182 / 187
页数:6
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