Biochar-based catalyst for simultaneous reactions of esterification and transesterification

被引:124
作者
Dehkhoda, Amir Mehdi [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; Transesterification; Esterification; Waste vegetable oil; Carbon-based catalyst; Biochar; SOLID ACID CATALYST; WASTE COOKING OIL; BIODIESEL PRODUCTION; HETEROGENEOUS CATALYSTS; CARBON; ACTIVATION; METHANOL; PHASE; KOH;
D O I
10.1016/j.cattod.2012.05.034
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Biochar, a by-product of fast pyrolysis of woody biomass, was developed as a renewable catalyst for simultaneous transesterification and esterification of canola oil and fatty acid (oleic acid) mixture at 150 degrees C under 1.52 MPa. Surface area and porosity of biochar were increased significantly from negligible to 990 m(2)/g, and 0.9 cm(3)/g through chemical activation method with KOH. The resultant biochar was sulfonated with fuming sulfuric acid to produce the biochar-based catalyst with high surface area and porosity (949 m(2)/g and 0.85 cm(3)/g). The ester formation yield was investigated based on the molar ratios of alcohol to canola oil (A:O), alcohol to oleic acid (A:FFA), or at constant mass ratio of alcohol to the mixture of oil and oleic acid. Increasing the FFA concentration from 15, 30 to 50 wt.% (at constant A: O molar ratio) resulted in slight increase of reaction yields from 27.9, 35.1, to 36.7%, respectively. Results also revealed a continuous increase in reaction yield from 38.0 to 48.1% as increasing A: FFA molar ratio (from 10: 1 to 30: 1) at constant A: O. However, increasing A: O ratio (from 10: 1 to 30: 1) at constant A: FFA resulted in an unexpected decrease in the reaction yield from 48.1 to 28.8%. The biochar based catalyst showed promising catalytic activity (48% yield in 3 h) for the combination of transesterification and esterification reactions in a mixture of canola oil and oleic acid for biodiesel production. Reaction yield decreased by similar to 8% upon reusing the catalyst. (C) 2012 Elsevier B. V. All rights reserved.
引用
收藏
页码:86 / 92
页数:7
相关论文
共 34 条
  • [1] Aldana-Perez A., FUEL
  • [2] Acid-catalyzed transesterification of canola oil to biodiesel under single- and two-phase reaction conditions
    Ataya, Fadi
    Dube, Marc A.
    Ternan, Marten
    [J]. ENERGY & FUELS, 2007, 21 (04) : 2450 - 2459
  • [3] Steam and KOH activation of biochar: Experimental and modeling studies
    Azargohar, R.
    Dalai, A. K.
    [J]. MICROPOROUS AND MESOPOROUS MATERIALS, 2008, 110 (2-3) : 413 - 421
  • [4] High performance heterogeneous catalyst for biodiesel production from vegetal and waste oil at low temperature
    Borges, M. E.
    Diaz, L.
    Alvarez-Galvan, M. C.
    Brito, A.
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2011, 102 (1-2) : 310 - 315
  • [5] Characterization of Biochar from Fast Pyrolysis and Gasification Systems
    Brewer, Catherine E.
    Schmidt-Rohr, Klaus
    Satrio, Justinus A.
    Brown, Robert C.
    [J]. ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 2009, 28 (03) : 386 - 396
  • [6] Canakci M, 2001, T ASAE, V44, P1429, DOI 10.13031/2013.7010
  • [7] Canakci M, 1999, T ASAE, V42, P1203, DOI 10.13031/2013.13285
  • [8] The potential of restaurant waste lipids as biodiesel feedstocks
    Canakci, Mustafa
    [J]. BIORESOURCE TECHNOLOGY, 2007, 98 (01) : 183 - 190
  • [9] Modern heterogeneous catalysts for biodiesel production: A comprehensive review
    Chouhan, A. P. Singh
    Sarma, A. K.
    [J]. RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2011, 15 (09) : 4378 - 4399
  • [10] Biochar based solid acid catalyst for biodiesel production
    Dehkhoda, Amir Mehdi
    West, Alex H.
    Ellis, Naoko
    [J]. APPLIED CATALYSIS A-GENERAL, 2010, 382 (02) : 197 - 204