Production of biodiesel using a continuous gas-liquid reactor

被引:49
作者
Behzadi, Sam [1 ]
Farid, Mohammed M. [1 ]
机构
[1] Univ Auckland, Dept Chem & Mat Engn, Auckland, New Zealand
关键词
Biodiesel; Methanol; Sodium methoxide; Sodium hydroxide; Spray reactor; METHYL-ESTERS; VEGETABLE-OILS; SOYBEAN OIL; SUNFLOWER OIL; FLOW REACTOR; TRANSESTERIFICATION; KINETICS; DISTILLATION; TALLOW; FUEL;
D O I
10.1016/j.biortech.2008.06.037
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A novel continuous reactor process has been developed for the production of biodiesel from fats and oils. The key feature of the process is its ability to operate continuously with a high reaction rate, potentially requiring less post reaction cleaning and product/reactant separation than currently established processes. This was achieved by atomising the heated oil/fat and then spraying it into a reaction chamber filled with methanol vapor in a counter current flow arrangement. This allows the continuous separation of product and the excess methanol stream in the reactor. The overall conversion based on a single cycle of this process has been between 50% and 96% of the feed stock materials. Conversions of 94-96% were achieved while operating with 5-7 g of sodium methoxide/L of methanol at methanol flow rate of 17.2 L/h and oil now rate of 10 L/h. Additional variations in the reactant stoichiometry (i.e. reactant flow rates), catalyst type/concentration, and reaction temperature on the overall product conversion were investigated. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:683 / 689
页数:7
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