Method for producing high-concentration alcohol
The present invention aims at providing a method for producing a high-concentration alcohol from a water-alcohol mixture, in which the overall process is efficient and the present invention relates to a production method of a high-concentration alcohol, including a water adsorption step of adsorbing water of a water-alcohol mixture on an adsorption column to obtain a first concentrated alcohol, a water desorption step of introducing an alcohol to obtain a hydrous alcohol, and a membrane separation step of introducing the hydrous alcohol into a membrane separation unit provided with a membrane composite containing zeolite having an SiO 2 /Al 2 O 3 molar ratio of 5 to 15 to obtain a second concentrated alcohol.
1. A method of concentrating ethanol, comprising
introducing a hydrous ethanol into a membrane separation unit that comprises a zeolite membrane comprising a zeolite with an SiO 2 /Al 2 O 3 molar ratio of 5 to 15 to obtain a concentrated ethanol having a concentration of at least 80% by mass of ethanol, wherein the membrane separation unit has a permeation of flux of water of 0.1 kg/(m 2 ·h) or more; and
dehydrating the concentrated ethanol with an LTA-type zeolite membrane.
2. The method of claim 1 , wherein the zeolite having an SiO 2 /Al 2 O 3 molar ratio of 5 to 15 is CHA-type zeolite.
3. The method of claim 1 , wherein the hydrous ethanol is obtained from alcohol fermentation with fermentative bacteria.
4. The method of claim 1 , wherein the hydrous ethanol further comprises an acid.
5. The method of claim 1 , wherein the concentrated ethanol has from 85% to 99.5% by mass of ethanol.
6. The method of claim 1 , wherein the concentrated ethanol has from 90% to 99.0% by mass of ethanol.
7. The method of claim 1 , wherein the concentrated ethanol has from 95% to 98.0% by mass of ethanol.
8. The method of claim 1 , wherein the membrane separation unit has a permeation of flux of water of 2.0 kg/(m 2 ·h) or more.
9. The method of claim 1 , wherein the membrane separation unit has a permeation of flux of water of 5.0 kg/(m 2 ·h) or more.
10. The method of claim 1 , wherein the hydrous ethanol further comprises an acid and the concentrated ethanol has from 85% to 99.5% by mass of ethanol.
11. The method of claim 1 , wherein the hydrous ethanol further comprises an acid,
the concentrated ethanol has from 85% to 99.5% by mass of ethanol, and the membrane separation unit has a permeation of flux of water of 2.0 kg/(m 2 ·h) or more.