Continuous Catalyst-Free Production of Biodiesel through Transesterification of Soybean Fried Oil in Supercritical Methanol and Ethanol

被引:65
|
作者
Gonzalez, Samantha L. [1 ]
Sychoski, Melania M. [2 ]
Navarro-Diaz, Helmut J. [1 ]
Callejas, Nicolas [3 ]
Saibene, Marcela [3 ]
Vieitez, Ignacio [3 ]
Jachmanian, Ivan [3 ]
da Silva, Camila [4 ]
Hense, Haiko [1 ]
Vladimir Oliveira, J. [1 ]
机构
[1] Univ Fed Santa Catarina, Dept Chem & Food Engn, BR-88040900 Florianopolis, SC, Brazil
[2] Univ Reg Integrada Alto Uruguai & Missoes URI, Dept Food Engn, BR-99700000 Erechim, RS, Brazil
[3] Univ Republica, Fac Quim, Lab Grasas & Aceites, Montevideo 11100, Uruguay
[4] Maringa State Univ UEM, Dept Technol, BR-87506370 Umuarama, Parana, Brazil
关键词
ACID ETHYL-ESTERS; WASTE COOKING OIL; FREE FATTY-ACIDS; VEGETABLE-OILS; RAPESEED OIL; METHYL ESTERIFICATION; KINETICS; FUEL; QUANTITATION; WATER;
D O I
10.1021/ef400869y
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
This work reports the production of fatty acid methyl esters (FAMEs) and fatty acid ethyl esters (FAEEs) by means of waste fried oil (WFO) transesterification using methanol and ethanol at supercritical conditions, in a continuous catalyst-free process. Transesterification experiments were performed from 573 to 623 K, at 10, 15, and 20 MPa, with oil/alcohol molar ratios of 1:20, 1:30, and 1:40 and water addition to alcohol of 0, 5, and 10 wt %. The extent of the reaction was explored using a novel parameter, convertibility, which corresponds to the maximum ester content attainable from the feedstock (92.1%). The highest FAME and FAEE contents achieved were 81.7 and 82.2%, respectively. Results show that transesterification of WFO in methanol was more efficient than that in ethanol, the temperature had the strongest influence, and the addition of water considerably improved the ester yield.
引用
收藏
页码:5253 / 5259
页数:7
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