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
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
作者
关键词
Biodiesel production process optimization, Reaction mechanism and kinetics, Mass transfer and diffusion, Mathematical model, Waste oil transesterification, Renewable energy and fuels
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