Modification of poly(vinyl alcohol) membranes using sulfur-succinic acid and its application to pervaporation separation of water-alcohol mixtures

• Published in: Journal of applied polymer science Vol. 68; no. 11; pp. 1717 - 1723
• Main Authors: Rhim, Ji-Won, Yeom, Choong-Kyun, Kim, Sun-Woo
• Format: Journal Article
• Language: English
• Published: New York John Wiley & Sons, Inc 13.06.1998; Wiley
• Subjects: Applied sciences; crosslinking; Exact sciences and technology; Exchange resins and membranes; Forms of application and semi-finished materials; pervaporation; poly(vinyl alcohol); Polymer industry, paints, wood; sulfur-succinic acid; Technology of polymers; Water; Transport properties; Vinyl ester copolymer; Vinyl alcohol copolymer; Crosslinking; Experimental study; Property processing relationship; Sulfonic acid; Primary alcohol; Crosslinked copolymer; Polyvinylalcohol; Selective permeability; Dicarboxylic acid; Membrane; Pervaporation
• ISSN: 0021-8995; 1097-4628
• DOI: 10.1002/(SICI)1097-4628(19980613)68:11<1717::AID-APP1>3.0.CO;2-M

For the purposes of the water‐selective membrane material development for pervaporation separation, we crosslinked poly(vinyl alcohol) (PVA) with sulfur‐succinic acid (SSA), which contains —SO3OH, by heat treatment and investigated the effect of the crosslinking density on the separation of water–alcohol mixtures by pervaporation technique. The crosslinking reaction between PVA and SSA was characterized through Fourier transform infrared spectroscopy and differential scanning calorimetry tests by varying the amount of the crosslinking agent, the reaction temperature, and the swelling measurements of each pure component. The separation performance of the water–methanol mixture is not good due to the existence of sulfonic acid, hydrophilic group, in the crosslinking agent. However, for the water–ethanol mixture, the flux of 0.291 kg/m2h and the separation factor of 171 were obtained at 70°C when PVA‐crosslinked membrane containing 7 wt % SSA was used. The same membrane also showed flux of 0.206 kg/m2h and a separation factor of 1969 at the same operating temperature. © 1998 John Wiley & Sons, Inc. J Appl Polym Sci 68: 1717–1723, 1998