Transesterification of oil to biodiesel in a continuous tubular reactor with static mixers: Modelling reaction kinetics, mass transfer, scale-up and optimization considering fatty acid composition
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- 作者：Blaž Likozar ; blaz.likozar@ki.si" class="auth_mail" title="E-mail the corresponding author ; Andrej Pohar ; Janez Levec
- 关键词：Biodiesel production process optimization ; Reaction mechanism and kinetics ; Mass transfer and diffusion ; Mathematical model ; Waste oil transesterification ; Renewable energy and fuels
- 刊名：Fuel Processing Technology
- 出版年：2016
- 出版时间：February 2016
- 年：2016
- 卷：142
- 期：Complete
- 页码：326-336
- 全文大小：1864 K
文摘
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Transesterification of oil to biodiesel in continuous reactor with static mixers
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Fatty acid composition of species proved to be detrimental in affecting reactivity.
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Simultaneous modelling of mass transfer, reaction kinetics and chemical equilibrium
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Distribution coefficients were significant upon non-determining mass transfer rate.
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Sensitivity analysis, scale-up, optimization, process intensification and economics