Optimization of biodiesel production process using sunflower oil and tetramethyl ammonium hydroxide as catalyst

被引:11
作者
Sanchez, B. S. [1 ]
Mendow, G. [1 ]
Levrand, P. G. [1 ]
Querini, C. A. [1 ]
机构
[1] Res Inst Catalysis & Petrochem INCAPE FIQ UNL CON, RA-3000 Santa Fe, Argentina
关键词
Transesterification; Tetramethyl ammonium hydroxide; Biodiesel; VEGETABLE-OILS; RAPESEED OIL; 2-STAGE TRANSESTERIFICATION; HETEROGENEOUS CATALYSTS; COOKING OIL; ESTERS; METHANOL; ETHANOL; YIELDS; AMINE;
D O I
10.1016/j.fuel.2013.05.085
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
In this work, the biodiesel production process by transesterification of sunflower oil was investigated using tetramethyl ammonium hydroxide (TMAH) as catalyst. The reaction conditions, such as catalyst concentration, temperature and reaction time were optimized in order to obtain a product that fulfills the quality requirements of international standards. It was found that the optimum reaction conditions were: temperature 60 degrees C, 1.76 wt% TMAH catalyst and 2 h reaction time. High amount of soaps were formed when using this catalyst. Therefore, an alternative purification methodology was used, especially useful for samples with high soaps content. This procedure consists of a first extraction stage using neutral water, which efficiently remove soaps. TMAH increases the solubility of mono and di-glycerides in the glycerine phase, thus decreasing their concentration in the biodiesel phase. Consequently, for a given production of mono-and di-glycerides, lower amount of these compounds were found in the final biodiesel product, being this an important advantage of this catalyst. (C) 2013 Elsevier Ltd. All rights reserved.
引用
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页码:323 / 330
页数:8
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