Zeolites for separation of ethanol and water

1. A process for separating ethanol from a mixture including ethanol and water, the process comprising:

contacting the mixture with a sorbent or membrane including one or more zeolites selected from the group consisting of:

an MRE-type zeolite, an MTT-type zeolite, an ATN-type zeolite, a ZON-type zeolite, an OWE-type zeolite, an ESV-type zeolite, a CGF-type zeolite, an MAZ-type zeolite, an STI-type zeolite, an AFO-type zeolite, an AEL-type zeolite, an ATO-type zeolite, or an EZT-type zeolite, wherein at least a fraction of the ethanol from the mixture is adsorbed by the sorbent or membrane and an unadsorbed portion of the mixture forms a raffinate having a lower concentration of ethanol than the mixture, wherein the one or more zeolites include a channel system wherein proximate and favorable ethanol adsorption sites are spatially separated by at least 0.35 nanometers to discourage hydrogen bonds between adsorbed ethanol molecules; and

releasing adsorbed ethanol from the sorbent or membrane as a retentate or a permeant to produce an ethanol extract having a higher concentration of ethanol than the mixture.

2. A process for separating ethanol from a mixture including ethanol and water, the process comprising:

contacting the mixture with a sorbent or membrane comprising one or more zeolites selected from the group consisting of an EAB-type zeolite or an SAT-type zeolite, wherein at least a fraction of the ethanol from the mixture is adsorbed by the sorbent or membrane and an unadsorbed portion of the mixture forms a raffinate having a lower concentration of ethanol than the mixture; and

releasing adsorbed ethanol from the sorbent or membrane as a retentate or a permeant to produce an ethanol extract having a higher concentration of ethanol than the mixture.

3. The process of claim 1 , wherein the one or more zeolites comprise a ratio of SiO 2 to Al 2 O 3 of at least about 20:1.

4. The process of claim 1 , wherein the one or more zeolites comprise a ratio of SiO 2 to Al 2 O 3 of at least about 50:1.

5. The process of claim 1 , wherein the raffinate remains above a concentration of about 1-5 wt % ethanol.

6. The process of claim 1 , wherein the one or more zeolites have an adsorption selectivity that is at least 80% of the selectivity required to yield an ethanol extract with a purity of at least 95.6 wt % ethanol.

7. The process of claim 1 , wherein the one or more zeolites have an ethanol adsorption capacity of at least 0.3 mol ethanol per kilogram of the zeolite sorbent or membrane when the raffinate is 1.5 wt % ethanol.

8. The process of claim 1 , wherein the one or more zeolites have an ethanol adsorption capacity of at least 0.8 mol ethanol per kilogram of the zeolite sorbent or membrane when the raffinate is 5 wt % ethanol.

9. A process for separating ethanol from a mixture including ethanol and water, the process comprising:

contacting the mixture with a sorbent or membrane comprising a VFI-type zeolite, wherein at least a fraction of the ethanol from the mixture is adsorbed by the sorbent or membrane and an unadsorbed portion of the mixture forms a raffinate, the raffinate having a lower concentration of ethanol than the mixture; and

releasing adsorbed ethanol from the sorbent or membrane as a retentate or a permeant to produce an ethanol extract having a higher concentration of ethanol than the mixture.

10. The process of claim 9 , wherein the raffinate reaches a concentration below about 1-3 wt % ethanol at the end of the process.

11. The process of claim 9 , wherein the VFI-type zeolite has an ethanol:water adsorption selectivity of at least 300:1 when the raffinate is 0.1 wt % ethanol.

12. The process of claim 9 , wherein the VFI-type zeolite has an ethanol adsorption capacity of at least 0.8 mol ethanol per kilogram of the zeolite sorbent or membrane when the raffinate is 0.1 wt % ethanol.

13. The process of claim 9 , wherein the VFI-type zeolite has an ethanol adsorption capacity of at least 1.5 mol ethanol per kilogram of the zeolite sorbent or membrane when the raffinate is 2 wt % ethanol.

14. The process of claim 1 , further comprising fermenting a fermentable feedstock to form a fermentation broth comprising ethanol and water, wherein the mixture comprises one or both of the fermentation broth or a vapor that forms above the fermentation broth.

15. The process of claim 2 , wherein the one or more zeolites comprise a ratio of SiO 2 to Al 2 O 3 of at least about 20:1.

16. The process of claim 2 , wherein the one or more zeolites comprise a ratio of SiO 2 to Al 2 O 3 of at least about 50:1.

17. The process of claim 2 , wherein the one or more zeolites have an adsorption selectivity that is at least 80% of the selectivity required to yield an ethanol extract with a purity of at least 95.6 wt % ethanol.

18. The process of claim 2 , wherein the one or more zeolites have an ethanol adsorption capacity of at least 0.3 mol ethanol per kilogram of the zeolite sorbent or membrane when the raffinate is 1.5 wt % ethanol.

19. The process of claim 2 , wherein the one or more zeolites have an ethanol adsorption capacity of at least 0.8 mol ethanol per kilogram of the zeolite sorbent or membrane when the raffinate is 5 wt % ethanol.

20. The process of claim 2 , further comprising fermenting a fermentable feedstock to form a fermentation broth comprising ethanol and water, wherein the mixture comprises one or both of the fermentation broth or a vapor that forms above the fermentation broth.

21. The process of claim 9 , further comprising fermenting a fermentable feedstock to form a fermentation broth comprising ethanol and water, wherein the mixture comprises one or both of the fermentation broth or a vapor that forms above the fermentation broth.