反应蒸馏
生物柴油
生物柴油生产
工艺工程
废物管理
可再生能源
环境科学
推流式反应器模型
蒸馏
制浆造纸工业
工程类
化学
化学工程
色谱法
连续搅拌釜式反应器
生物化学
电气工程
催化作用
作者
R. J. M. C. L. Silva,Thibério Pinho Costa Souza,J. P. Silva,José Geraldo A. Pacheco,JULIA MIRANDA SILVA
标识
DOI:10.1590/0104-6632.20170343s20150691
摘要
The interest in biodiesel as an alternative source of energy has been extremely intensified by its use as a renewable and economically viable fuel. As a result, continuous production processes have been a requirement to supply growing demand. This work presents experimental and simulated results of two biodiesel production pilot plants and makes a comparison between the processes they use. The first one was designed with three plug flow reactors (PFRs) connected with recycle streams. The second one was composed of a reactive distillation process for biodiesel production. Repeated tests in Aspen Plus and Matlab showed that multiple PFRs with high volume are required for 98% ester conversion. However, a single unit of reactive distillation resulted in 99% conversion. In short, to produce large quantities of biodiesel this work indicates continuous reactive distillation as the most adequate process.
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