Methanol-enhanced chemical interesterification of sunflower oil with methyl acetate

被引:30
作者
Casas, Abraham [1 ]
Jesus Ramos, Maria [1 ]
Perez, Angel [1 ]
机构
[1] Univ Castilla La Mancha, Inst Chem & Environm Technol ITQUIMA, Dept Chem Engn, E-13071 Ciudad Real, Spain
关键词
Chemical interesterification; Sunflower oil; Methyl acetate; FAME; Triacetin; BIODIESEL PRODUCTION; TRANSESTERIFICATION; TRIACETIN;
D O I
10.1016/j.fuel.2012.11.037
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The aim of this work was to investigate the commercial mixture of methanolic potassium methoxide as catalyst in chemical interesterification of sunflower oil with methyl acetate. The presence of methanol significantly enhanced the reaction process because it increased the reaction rate, improved the safety of the process and facilitated the manipulation of the catalyst. The reactions were performed at 50 degrees C using a methyl acetate-to-oil molar ratio (MAOMR) of 12-48 and a catalyst-to-oil molar ratio (COMR) of 0.1-0.2. The optimum conditions were achieved with the MAOMR of 48 and the COMR of 0.1 and the final product composition was: fatty acid methyl esters (77.0 wt.%), triacetin (12.1 wt.%), diacetinmonoglyceride (4.0 wt.%) and diacetin, monoacetin and glycerol fraction (6.8 wt.%). Finally, technical feasibility of the intermediate diacetinmonoglyceride elimination through the addition of higher amounts of methanol was also evaluated. (c) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:869 / 872
页数:4
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