skip to main content
OSTI.GOV title logo U.S. Department of Energy
Office of Scientific and Technical Information

Title: Some characteristics of pervaporation for dilute ethanol-water mixtures by alcohol-permselective composite membrane

Journal Article · · Separation Science and Technology
OSTI ID:494261

Zeolite-filled polydimethylsiloxane/polysulfone composite membranes were prepared and used to separate ethanol from dilute ethanol-water mixtures through a pervaporation process. During this process the relationship between flux (J) and temperature (T) is J = 597.95 exp(-E{sub o}/RT)(g/m{sup 2}{center_dot}h), E{sub o} = 3.292 kJ/mol. The experimental results show that the flux decreases with increasing downstream pressure while the selectivity ({alpha}{sub EtOH/Water}) rises, the flux increases, and the selectivity decreases with a rise of feed concentration, and the flux as well as the selectivity increase with increasing bulk velocity on the upstream side of the membrane.

OSTI ID:
494261
Journal Information:
Separation Science and Technology, Vol. 31, Issue 20; Other Information: PBD: Dec 1996
Country of Publication:
United States
Language:
English

Similar Records

Concentration of dilute acetone-water solutions using pervaporation
Journal Article · Mon Mar 01 00:00:00 EST 1993 · Separation Science and Technology; (United States) · OSTI ID:494261

Pervaporation of aqueous ethanol mixtures through poly(dimethyl siloxane) membranes
Journal Article · · Separation Science and Technology; (United States) · OSTI ID:494261

A high performance membrane for sorption and pervaporation separation of ethyl tert-butyl ether and ethanol mixtures
Journal Article · Mon Feb 01 00:00:00 EST 1999 · Separation Science and Technology · OSTI ID:494261