Esterification pretreatment of free fatty acid in biodiesel production, from laboratory to industry

被引:195
|
作者
Chai, Ming [1 ]
Tu, Qingshi [2 ]
Lu, Mingming [2 ]
Yang, Y. Jeffrey [3 ]
机构
[1] Greenleaf Biofuels, New Haven, CT 06512 USA
[2] Univ Cincinnati, Sch Energy Environm Biol & Med Engn, Cincinnati, OH 45221 USA
[3] US EPA, Natl Risk Management Res Labs, Cincinnati, OH 45221 USA
基金
美国国家科学基金会;
关键词
Acid-catalyzed esterification; Biodiesel; Used cooking oil; Free fatty acid; Methanol to FFA ratio; Optimization; WASTE COOKING OIL; RUBBER SEED OIL; CRUDE PALM OIL; JATROPHA-CURCAS; OPTIMIZATION; CATALYST; KINETICS; WATER; FUEL; FFA;
D O I
10.1016/j.fuproc.2014.03.025
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In the US, biodiesel producers usually follow the 19.8:1 methanol-to-FFA molar ratio for free fatty acid (FFA) esterification, as suggested by the National Renewable Energy Laboratory (NREL) without optimization studies. In this paper, both laboratory studies and industrial practices of the esterification process were compared, and an optimization study of a used vegetable oil with 5% FFA was conducted. The optimal conditions of this oil, i.e., methanol-to-FFA molar ratio of 40:1, and sulfuric acid usage of 10%, fell out of the suggested range of 19.8:1. The activation energy of the esterification reaction is 20.7 kJ/mol at the optimized condition and 45.9 kJ/mol at the 19.8:1 methanol to FFA ratio. It was found that the 19.8:1 methanol-to-FFA molar ratio worked well only within the FFA range of 15-25% while the suggested 5% sulfuric acid worked well only within the FFA range of 15-35%. Outside these ranges, especially at FFA levels less than 15%, optimization study is necessary. Regression models of methanol and acid dosing have been utilized in two industrial scale biodiesel producing facilities and have successfully reduced the FFA level to less than 0.5%. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:106 / 113
页数:8
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