Fawzy Mohamed K, Varela-Corredor Felipe, Bandini Serena
Department of Civil, Chemical, Environmental and Materials Engineering (DICAM)-Alma Mater Studiorum, University of Bologna, I-40136 Bologna, Italy.
Membranes (Basel). 2019 Sep 23;9(10):125. doi: 10.3390/membranes9100125.
The paper introduces some aspects of the characterization of hydrophobized multilayer ceramic membranes intended for use in membrane distillation (MD) operations. Four-layer hydrophobic carbon-based titania membranes, manufactured by the Fraunhofer Institute for Ceramic Technologies and Systems (IKTS, Hermsdorf, Germany), were tested according to the gas permeation technique. Gas permeance data were elaborated following the premises of the dusty gas model, to calculate the average pore size and the porosity-tortuosity ratio of each layer. Membrane testing was the opportunity to discuss which characterization method is more appropriate to obtain the membrane parameters necessary for the simulation of membranes in MD processes. In the case of multilayer membranes, the calculation of the morphological parameters should be performed for each layer. The "layer-by-layer gas permeation" method, previously introduced by other authors and completed in this work, is more appropriate for obtaining representative parameters of the membrane. Conversely, the calculation of morphological parameters, averaged over the entire membrane, might lead to heavy underestimations of the total membrane resistance and then to a heavy error on the transmembrane flux simulation.
本文介绍了用于膜蒸馏(MD)操作的疏水化多层陶瓷膜的一些表征方面。由弗劳恩霍夫陶瓷技术与系统研究所(德国赫姆斯多夫的IKTS)制造的四层疏水碳基二氧化钛膜,根据气体渗透技术进行了测试。按照含尘气体模型的前提对气体渗透数据进行了详细分析,以计算每层的平均孔径和孔隙率-曲折度比。膜测试提供了一个契机,来讨论哪种表征方法更适合获取MD过程中膜模拟所需的膜参数。对于多层膜,应针对每层进行形态学参数的计算。先前由其他作者提出并在本工作中完善的“逐层气体渗透”方法,更适合于获取膜的代表性参数。相反,对整个膜平均的形态学参数计算,可能会导致对总膜阻力的严重低估,进而在跨膜通量模拟上产生严重误差。