초록 ▼

A process for producing anhydrous ethanol from an ethanol-water mixture feedstock comprising subjecting the feedstock to distillation in a first distillation zone to produce an overhead vapor of from about 80 to about 90 weight percent ethanol, subjecting the thus produced overhead vapor to extracti

A process for producing anhydrous ethanol from an ethanol-water mixture feedstock comprising subjecting the feedstock to distillation in a first distillation zone to produce an overhead vapor of from about 80 to about 90 weight percent ethanol, subjecting the thus produced overhead vapor to extractive distillation in an extractive distillation zone to produce anhydrous ethanol vapor overhead of about 99.5 weight percent ethanol and a solvent-rich bottom stream, and stripping the solvent-rich bottom stream and recycling the thus produced lean solvent bottom stream to the extractive distillation zone and recycling the thus produced overhead vapor stream to the first distillation zone. Also disclosed is a system for performing the process.

대표청구항 ▼

1. A process for dehydrating an aqueous feedstock comprising water and ethanol, comprising: distilling said feedstock under distillation conditions in a first distillation zone to produce a first liquid bottoms product and a first vapor overhead stream comprising ethanol and water; introducing a

1. A process for dehydrating an aqueous feedstock comprising water and ethanol, comprising: distilling said feedstock under distillation conditions in a first distillation zone to produce a first liquid bottoms product and a first vapor overhead stream comprising ethanol and water; introducing at least a portion of said first vapor overhead stream into an extractive distillation zone; contacting said thus introduced first vapor overhead with a selective solvent in said extractive distillation zone under extractive distillation conditions to thereby produce a second liquid bottoms product comprising water and said selective solvent and to thereby produce a second vapor overhead stream comprising greater than 95.57 weight percent ethanol based on the total weight of said second vapor overhead; introducing at least a portion of said second liquid bottoms product comprising water and said selective solvent into a solvent stripper zone; separating said second bottoms product under solvent stripping conditions in said solvent stripper zone into a third vapor overhead stream comprising water and ethanol and a third liquid bottoms product comprising said selective solvent; and introducing at least a portion of said third vapor overhead stream into said first distillation zone. 2. A process in accordance with claim 1 wherein said solvent stripping conditions include a subatmospheric pressure. 3. A process in accordance with claim 1 wherein said solvent stripping conditions include a temperature above the boiling point of water and below the boiling point of said selective solvent. 4. A process in accordance with claim 1 wherein said selective solvent consists essentially of a composition selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, trimethylene glycol, glycerin, sulfolane, 1,4-butandediol, N-methyl pyrrolidone, phenylthioethanol, di-n-propyl sulfone, and combinations of any two or more thereof. 5. A process in accordance with claim 1 wherein said selective solvent consists essentially of ethylene glycol. 6. A process in accordance with claim 1 wherein said selective solvent consists essentially of glycerin. 7. A process in accordance with claim 1 characterized further to include: introducing at least a portion of said third bottoms product stream into said extractive distillation zone. 8. A process in accordance with claim 7 wherein said feedstock consists essentially of fermentation broth. 9. A process in accordance wtih claim 1 wherein said feedstock consists essentially of fermentation broth and said selective solvent consists essentially of a composition selected from the group consisting of ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, trimethylene glycol, glycerin, sulfolane, 1,4-butanediol, N-methyl pyrrolidone, phenylthioethanol, di-n-propyl sulfone, and combinations of any two or more thereof. 10. A process in accordance with claim 1 wherein said feedstock comprises no more than about 14 weight percent ethanol based on the total weight of the feedstock. 11. A process in accordance with claim 1 wherein said first vapor overhead comprises no more than about 90 weight percent ethanol based on the total weight of said first vapor overhead. 12. A process in accordance with claim 1 wherein said first vapor overhead comprises ethabol in the range from about 85 to about 90 weight percent based on the total weight of said first vapor overhead. 13. A process in accordance with claim 1 wherein said second vapor overhead comprises at least about 99 weight percent ethanol based on the total weight of said second vapor overhead. 14. A process in accordance with claim 1 wherein said second vapor overhead comprises at least about 99.5 weight percent ethanol based on the total weight of said second vapor overhead. 15. A process in accordance with claim 1 wherein said aqueous feedstock consists essentially of fermentation broth.