Ultrafast Biodiesel Production Using Ultrasound in Batch and Continuous Reactors

被引:49
作者
Boffito, D. C. [2 ]
Mansi, S. [1 ]
Leveque, J. -M. [3 ]
Pirola, C. [1 ]
Bianchi, C. L. [1 ]
Patience, G. S. [2 ]
机构
[1] Univ Milan, Dipartimento Chim, I-20133 Milan, Italy
[2] Polytech Montreal, Dept Genie Chim 2900, Montreal, PQ H3T 1J4, Canada
[3] Univ Savoie, LCME CISM, F-73376 Le Bourget Du Lac, France
关键词
Biodiesel production; Transesterification; Hydrodynamic cavitation; Acoustic cavitation; Rosett cell; Continuous reactor; IN-SITU TRANSESTERIFICATION; OF-THE-ART; OIL; INTENSIFICATION; OPTIMIZATION; ESTERIFICATION; ACIDS;
D O I
10.1021/sc400161s
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Biodiesel is produced in multi-stage batch reactors in which mass transfer is a rate limiting step. Mass transfer rates may be accelerated with ultrasound (US). In this paper, the performance of continuous flow US reactors, a Rosett US cell reactor, and a batch US reactor are compared to a conventional mechanically stirred batch reactor. The Rosett cell reactor combines acoustic cavitation and turbulence and achieved biodiesel yields greater than 90% in 5 min, whereas the same level of performance in the conventional reactor took more than 90 min. The most significant result of this work lies in achieving biodiesel yields greater than 90% after a single passage of the reagents in a continuous flow reactor in the presence of pulsed ultrasound. This corresponds to a reaction time of 18 s and a rate 300 times faster than the conventional process.
引用
收藏
页码:1432 / 1439
页数:8
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