Production of biodiesel from microalgae oil (Chlorella protothecoides) by non-catalytic transesterification: Evaluation of reaction kinetic models and phase behavior

被引:28
|
作者
Liu, Jiuxu [1 ]
Lin, Ronghong [1 ]
Nan, Yue [1 ]
Tavlarides, Lawrence L. [1 ]
机构
[1] Syracuse Univ, Dept Biomed & Chem Engn, Syracuse, NY 13244 USA
来源
关键词
Biodiesel; Microalgae oil; Non-catalytic transesterification; Phase behavior; Reaction kinetic models evaluation; RBD PALM OIL; SUPERCRITICAL TRANSESTERIFICATION; THERMAL-DECOMPOSITION; RAPESEED OIL; EQUILIBRIA; TRIGLYCERIDES; MIXTURES; COST; ALCOHOLS; ESTERS;
D O I
10.1016/j.supflu.2015.01.010
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 non-catalytic transesterification of microalgae oil with methanol was conducted at 300-400 degrees C, 150-300 bar, methanol-to-oil molar ratio (MOMR) of 6-12, and residence time of 0.5-10 min. A visualization system was built to study the phase transition, and it shows that at the conditions (T: 300-400 degrees C, P: 200 bar, tau: 0.5-10 min, MOMR of 9), the reactions were performed in homogeneous state. The dynamic phase behavior of the reacting systems was also investigated by RK-Aspen Equation of State. The results indicate that at 200 bar, MOMR of 9, and 300-385 degrees C, the reacting mixtures were in liquid state and moved toward supercritical region, while at 400 degrees C the reacting system was initially in liquid state and quickly approached supercritical state due to the fast reaction conversion. The critical points of the reaction mixtures were estimated. Ten commonly used kinetic models were evaluated, and it shows that three-step, reversible second-order model worked best in the data fitting. Reaction rate constants and activation energies for selected models were determined and compared with literature data. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:38 / 50
页数:13
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