US 5,294,304 AGranted

Process for the recovery of absolute ethanol by vapor compression extractive distillation

AssigneeMinistry of International Trade & Industry

InventorsYoshikazu Kano, Hirotoshi Horizoe, Tetsuya Tanimoto, Itsuo Yamamoto

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Abstract

This invention relates to a process for the production of absolute alcohol from aqueous alcohol, whereby saving of energy to a greater extent is rendered possible in a more simple process, as compared with the prior art azeotropic distillation method using benzene or cyclohexane. That is, aqueous alcohol is subjected to extractive distillation in a first distillation column under such a condition that a liquid and gas of a solvent simultaneously coexist using low pressure propane, propylene and butane as the solvent, absolute alcohol substantially free from water is recovered from the bottom of the distillation column and subjected to stripping of hydrocarbons in a second distillation column, during which the gaseous phases of the first and second distillation columns are mixed and compressed, utilized through recompression as a heat source of a reboiler of the first distillation column, subjected to separation of water content and recycled to the upper parts of the first and second distillation columns. In accordance with the process, the energy required can largely be reduced. In Examples, the energy required for producing 1 kg of absolute alcohol is reduced to 1/5 to 1/10 of the prior art azeotropic distillation method, which shows the advantages of the present invention. According to the process of the present invention, installations such as compressors, heat exchangers, decanters, etc. can be omitted and the installation cost can be reduced by about 30%.

Claims1

Dependent claims

A process for the production of absolute ethanol, which comprises

feeding a raw material containing ethanol and water, as predominant components, to the middle part of a first distillation column,
feeding a hydrocarbon solvent to the upper part of the first distillation column, maintaining the hydrocarbon solvent at such a temperature and pressure that a liquid phase and a gas phase of the hydrocarbon solvent are simultaneously present in the first distillation column,
withdrawing a liquid mixture comprising ethanol and hydrocarbon solvent, substantially free from water content, from the bottom of the first distillation column,
withdrawing a first gas comprising water and hydrocarbon solvent, substantially free from ethanol, from the top of the first distillation column,
feeding the liquid mixture of ethanol and hydrocarbon solvent from the bottom of the first distillation column into a second distillation column,
stripping the hydrocarbon solvent from the ethanol in the second distillation column and withdrawing absolute ethanol from the bottom of the second distillation column;
withdrawing a second gas comprising hydrocarbon solvent from the top of the second distillation column and forming a gaseous mixture with the first gas from the top of the first distillation column,
compressing the gaseous mixture of the first and second gases and using at least some of the recompression heat thereby produced as a heat source for the first distillation column,
cooling and liquifying the gaseous mixture of the first and second gases,
separating the hydrocarbon solvent from the water in the liquified gaseous mixture, and
recycling the hydrocarbon solvent into the upper parts of the first and second distillation columns.

8 more elements

Dependencies are inferred from the claim text.