Biochar based solid acid catalyst for biodiesel production

被引:302
|
作者
Dehkhoda, Amir Mehdi [1 ]
West, Alex H. [1 ]
Ellis, Naoko [1 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V6T 1Z3, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Biodiesel; Heterogeneous acid catalyst; Biochar; Esterification; Transesterification; RAPESEED OIL; FATTY-ACIDS; CARBON; TRANSESTERIFICATION; ESTERIFICATION; ACTIVATION; PYROLYSIS; FUEL;
D O I
10.1016/j.apcata.2010.04.051
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
A promising catalyst based on a biomass pyrolysis by-product, biochar, has been developed for the production of biodiesel. Two carbon-based solid acid catalysts were prepared by sulfonating pyrolysis char with concentrated or fuming sulfuric acids. Prepared catalysts were studied for their ability to catalyze transesterification of vegetable oils and esterification of free fatty acids. The catalyst sulfonated with the concentrated sulfuric acid demonstrated considerable conversion in free fatty acid esterification, while indicating limited transesterification activity. Using the stronger sulfonating reagent, fuming sulfuric acid, resulted in much higher transesterification activity. Further investigation of the latter catalyst was conducted to determine the effect of sulfonation time (5 and 15 h) and surface area on the transesterification reaction. The surface area of the biochar was increased by chemical treatment using 10 M potassium hydroxide through porosity development. The resulting four catalysts were compared for their catalytic activity. Results showed the catalyst with the highest surface area and acid density to have the highest catalytic activity for the production of biodiesel from canola oil in the presence of methanol as the reagent. Furthermore, the catalyst with the higher surface area indicated higher transesterification activity among the catalyst with similar acid densities. The effects of alcohol to oil (A:O) molar ratio, reaction time and catalyst loading on the esterification reaction catalyzed by the sulfonated biochar were also investigated. Free fatty acid (FFA) conversion increased with increasing A:O molar ratio, reaction time and catalyst loading. The catalyst has a tremendous potential to be used in a process converting a high FFA feedstock to biodiesel. (c) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:197 / 204
页数:8
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