Optimization of the reaction parameters for fast pseudo single-phase transesterification of sunflower oil

被引:42
|
作者
Casas, Abraham [1 ]
Maria Fernandez, Carmen [1 ]
Jesus Ramos, Maria [1 ]
Perez, Angel [1 ]
Francisco Rodriguez, Juan [1 ]
机构
[1] Univ Castilla La Mancha, Dept Chem Engn, Inst Chem & Environm Technol ITQUIMA, E-13071 Ciudad Real, Spain
关键词
Biodiesel; Pseudo single-phase; Cosolvent; Response surface; Factorial design; RESPONSE-SURFACE METHODOLOGY; INTEGRATED BIODIESEL PRODUCTION; ACID METHYL-ESTERS; SOYBEAN OIL; RAPESEED OIL; CATALYZED METHANOLYSIS; VEGETABLE-OILS; FUEL; TRANSMETHYLATION; MIXTURES;
D O I
10.1016/j.fuel.2009.08.004
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
Transesterification of sunflower oil with methanol was carried out using potassium hydroxide and methoxide as catalysts and MTBE as cosolvent. The aim of this work was to study and optimize the reaction parameters. Chosen parameters were reaction time, catalyst amount and methanol amount ( expressed as catalyst-to-oil and methanol-to-oil molar ratios, respectively). The response variables were methyl ester content (ME) and acid value (AV) due to their relationship with the completion and yield reaction, respectively. A factorial plus composite design was developed to carry out the optimization. From this design, several quadratic models have been used to fit the experimental data. All the factors studied had a positive influence on methyl ester content and acid value, except the methanol amount on acid value. For methoxide catalyst, optimum values were 0.235 catalyst to oil molar ratio, 12 methanol to oil molar ratio and 5 min reaching 99 wt.% ME and 0.20 mg KOH/g of AV. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:650 / 658
页数:9
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