Department of Chemical Engineering, Laboratory of Applied Physical Chemistry and Environmental Technology, K.U. Leuven, W. de Croylaan 46, B-3001 Leuven, Belgium.
Bioresour Technol. 2011 Jan;102(2):1669-74. doi: 10.1016/j.biortech.2010.09.092. Epub 2010 Sep 29.
Pervaporation is claimed to be a promising separation technique for the purification of ethanol from fermentation broths during bio-ethanol production. In this study, influence of fermentation by-products on the purification of ethanol from water during hydrophobic pervaporation was investigated. Sugars and salts were found to increase the membrane performance. Reason for this was a change in vapor/liquid equilibrium. 2,3-butanediol decreased the ethanol flux and selectivity factor, while glycerol exhibited no effect. This was explained by a strong sorption of butanediol into PDMS and no sorption of glycerol. Due to the presence of carboxylic acids, hydrophobicity degree of the Pervap 4060 membrane decreased, which resulted in an irreversible increase in water flux and decrease in separation performance. These observations suggested the presence of silicalite-based fillers in the membrane. When the pH was raised to a value above the dissociation constant, no changes in hydrophobicity degree and membrane performance were found.
渗透汽化被认为是一种很有前途的分离技术,可以在生物乙醇生产过程中从发酵液中提纯乙醇。在这项研究中,考察了发酵副产物对疏水性渗透汽化过程中从水中提纯乙醇的影响。发现糖和盐会提高膜性能。原因是蒸汽/液体平衡发生了变化。2,3-丁二醇降低了乙醇通量和选择性因子,而甘油则没有影响。这是由于丁二醇在 PDMS 中的强烈吸附和甘油的不吸附所致。由于存在羧酸,Pervap 4060 膜的疏水性降低,导致水通量不可逆增加,分离性能下降。这些观察结果表明膜中存在基于硅沸石的填料。当 pH 值升高到离解常数以上时,疏水性和膜性能没有变化。