Low-energy extractive distillation process for dehydration...

Distillation: processes – separatory – Distilling to separate or remove only water – From organic compound

Reexamination Certificate

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C203S001000, C203S002000, C203S022000, C203S023000, C203S060000, C203S062000, C203S064000, C203S065000, C203S074000, C203S075000, C203S078000, C203S087000, C203S099000, C203SDIG013, C203SDIG019, C426S492000, C426S493000, C426S494000, C568S916000

Reexamination Certificate

active

08002953

ABSTRACT:
An energy-efficient extractive distillation process for producing anhydrous ethanol from aqueous/ethanol feeds containing any range of ethanol employs an extractive distillation column (EDC) that operates under no or greatly reduced liquid reflux conditions. The EDC can be incorporated into an integrated process for producing anhydrous ethanol used for gasoline blending from fermentation broth. By using a high-boiling extractive distillation solvent, no solvent is entrained by the vapor phase to the EDC overhead stream, even under no liquid reflux conditions. The energy requirement and severity of the EDC can be further improved by limiting ethanol recovery in the EDC. In this partial ethanol recovery design, ethanol which remains in the aqueous stream from the EDC is recovered in a post-distillation column or the aqueous stream is recycled to a front-end pre-distillation column where the ethanol is readily recovered since the VLE curve for ethanol/water is extremely favorable for distillation.

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PCT/US2008/008223 Notification of transmittal of the International Search Report and Written Opinion, Feb. 10, 2009.
Lee et al, “Two-Liquid-Phase extractive distillation for aromatics recovery” Ind. Eng. Chem. Res., vol. 26, No. 3, (pp. 564-573)1987.
Drickamer & Hummel, “Application of experimental vapor-liquid equilibria to an analysis of the operation of a commercial unit for the purification of toluene from petroleum” Transactions of the Am. Institute of Chem Eng. 41, pp. 607-629 (1945).

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