Tuesday, November 10, 2009
Ryman Hall B1/B2 (Gaylord Opryland Hotel)
In this work, we propose a rigorous model for bioethanol dehydration process with supercritical propane to minimize costs. Thermodynamic predictions are performed with an upgraded Group Contribution with Association Equation of State, GCA-EOS. As compared to the basic scheme for dehydration with supercritical fluids, vapor recompression, as well as feed preconcentration could be highly energy efficient. We further consider alternative integration schemes between process streams, associated to different nonlinear programming problems. Special attention has been devoted to a new scheme that integrates the vapor recompression scheme to the preconcentration step, which provides additional reduction in total energy consumption. We demonstrate that bioethanol dehydration can be a sustainable alternative that is energetically competitive with molecular sieves in the production of this biofuel
See more of this Session: Poster Session: General On Separations
See more of this Group/Topical: Separations Division
See more of this Group/Topical: Separations Division
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