Use of heterogeneous acid catalyst combined with pressurized conditions for esters production from macauba pulp oil and methyl acetate

被引:20
|
作者
Visioli, Luiz Jardel [1 ,2 ]
de Castilhos, Fernanda [2 ]
da Silva, Camila [1 ,3 ]
机构
[1] Univ Estadual Maringa, Programa Posgrad Engn Quim, Ave Colombo 5790, BR-87020900 Maringa, Parana, Brazil
[2] Univ Fed Santa Maria, Programa Posgrad Engn Quim, Ave Roraima 1000, BR-97105900 Santa Maria, RS, Brazil
[3] UEM, Dept Tecnol, Ave Angelo Moreira da Fonseca 180, BR-87506370 Umuarama, PR, Brazil
来源
关键词
gamma-Alumina; Triacetin; Biodiesel; Continuous production; Glycerol free; BIODIESEL PRODUCTION; ACROCOMIA-ACULEATA; FEEDSTOCK; INTERESTERIFICATION; OPTIMIZATION; PERFORMANCE; TRIACETIN; ADDITIVES; ALUMINA; REACTOR;
D O I
10.1016/j.supflu.2019.03.023
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
The objective of this work was to evaluate the production of fatty acid methyl esters using macauba oil and methyl acetate under pressurized conditions, using heterogeneous gamma-alumina catalyst in a continuous system. The catalytic reaction kinetics were evaluated at temperatures between 225 and 300 degrees C, as well as the effect of catalyst particle size on the reaction. The temperature increase promoted an esters and triacetin (TA) production rise. It was found that the catalyst utilization, in granulometry from 0.85 to 1.00 mm, allowed better product yields at shorter residence time. The best result for catalytic reaction was obtained using the smallest catalyst particle size (0.85-1 mm), 275 degrees C, 20 MPa, methyl acetate (MA):oil mass ratio of 2.5:1, 20 min, obtaining 60.24 +/- 0.68% esters content and 2.76 +/- 0.06% TA content. The heterogeneous catalyst usage increased the TA production by 736% and the esters production by 33%. (C) 2019 Elsevier B.V. All rights reserved.
引用
收藏
页码:65 / 74
页数:10
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