Base-Catalyzed Ethanolysis of Waste Cooking Oil in a Micro/Millireactor System: Flow and Reaction Analysis

被引:5
|
作者
Borovinskaya, Ekaterina S. [1 ]
Sabaditsch, Daniel [1 ]
Reschetilowski, Wladimir [1 ]
机构
[1] Univ Technol Dresden, Inst Ind Chem, Helmholtzstr 16, D-01069 Dresden, Germany
关键词
Biodiesel; Ethanolysis; Flow analysis; Micro/millireactor; Waste cooking oil; FREE FATTY-ACID; BIODIESEL PRODUCTION; SOYBEAN OIL; SUNFLOWER OIL; TRANSESTERIFICATION; ESTERIFICATION; OPTIMIZATION; KINETICS; DESIGN;
D O I
10.1002/ceat.201800704
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
An important way for the production of biodiesel is the base-catalyzed transesterification of oil or fat with monohydric alcohols. Flow and reaction analysis with respect to the applicability of a micro/millireactor setup to two-phase ethanolysis of waste cooking oil is described. The flow in the micro/millireactor system was examined on the example of a soybean oil/ethanol mixture and compared with a T-mixer. Parallel and slug flow were observed in different reactor sections of the micro/milli-reactor system and evaluated concerning their efficiency. A method for determination of the viscosity of the mixture was conducted and validated. Certain pretreatments were investigated with regard to the suitability of the waste cooking oil for ethanolysis. Relations between biodiesel yields and some oil properties like chain length and acid number were found.
引用
收藏
页码:495 / 505
页数:11
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