Enzymatic conversion of corn oil into biodiesel in a batch supercritical carbon dioxide reactor and kinetic modeling

被引:54
作者
Ciftci, Ozan Nazim [1 ]
Temelli, Feral [1 ]
机构
[1] Univ Alberta, Dept Agr Food & Nutr Sci, Edmonton, AB T6G 2P5, Canada
关键词
Batch bioreactor; Biodiesel; Enzymatic alcoholysis; Lipase; Supercritical carbon dioxide; LIPASE-CATALYZED METHANOLYSIS; CANDIDA-ANTARCTICA LIPASE; ESTER SYNTHESIS; CANOLA OIL; PALM OIL; TRANSESTERIFICATION; TRIGLYCERIDES; OPTIMIZATION; HYDROLYSIS; ALCOHOLS;
D O I
10.1016/j.supflu.2012.12.029
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
Synthesis of fatty acid methyl esters (FAME) as biodiesel from corn oil was studied in a batch supercritical carbon dioxide (SC-CO2) bioreactor using immobilized lipase (Novozym 435) as catalyst. Effects of reaction conditions on the contents of FAME, monoacylglycerols (MAG), diacylglycerols (DAG), and triacyglycerols (TAG) were investigated at various enzyme loads (5-15%), temperatures (40-60 degrees C), substrate mole ratios (corn oil:methanol; 1:3-1:9), pressures (10-30 MPa), and times (1-8 h). The highest FAME content (81.3%) was obtained at 15% enzyme load, 60 degrees C, 1:6 substrate mole ratio, and 10 MPa in 4 h. A reaction kinetic model was used to describe the system, and the activation energy of the system was calculated as 72.9 kJ/mol. Elimination of the use of organic solvents, chemical catalysts and wastewater as well as reasonably high yields make the enzymatic synthesis of biodiesel in SC-CO2 a promising green alternative to conventional biodiesel process. (c) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:172 / 180
页数:9
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