Zamani Ali, Tezel F Handan, Thibault Jules
Department of Chemical and Biological Engineering, University of Ottawa, Ottawa, ON K1N 6N5, Canada.
Membranes (Basel). 2021 Jan 14;11(1):58. doi: 10.3390/membranes11010058.
Membrane-based processes are considered a promising separation method for many chemical and environmental applications such as pervaporation and gas separation. Numerous polymeric membranes have been used for these processes due to their good transport properties, ease of fabrication, and relatively low fabrication cost per unit membrane area. However, these types of membranes are suffering from the trade-off between permeability and selectivity. Mixed-matrix membranes, comprising a filler phase embedded into a polymer matrix, have emerged in an attempt to partly overcome some of the limitations of conventional polymer and inorganic membranes. Among them, membranes incorporating tubular fillers are new nanomaterials having the potential to transcend Robeson's upper bound. Aligning nanotubes in the host polymer matrix in the permeation direction could lead to a significant improvement in membrane permeability. However, although much effort has been devoted to experimentally evaluating nanotube mixed-matrix membranes, their modelling is mostly based on early theories for mass transport in composite membranes. In this study, the effective permeability of mixed-matrix membranes with tubular fillers was estimated from the steady-state concentration profile within the membrane, calculated by solving the Fick diffusion equation numerically. Using this approach, the effects of various structural parameters, including the tubular filler volume fraction, orientation, length-to-diameter aspect ratio, and permeability ratio were assessed. Enhanced relative permeability was obtained with vertically aligned nanotubes. The relative permeability increased with the filler-polymer permeability ratio, filler volume fraction, and the length-to-diameter aspect ratio. For water-butanol separation, mixed-matrix membranes using polydimethylsiloxane with nanotubes did not lead to performance enhancement in terms of permeability and selectivity. The results were then compared with analytical prediction models such as the Maxwell, Hamilton-Crosser and Kang-Jones-Nair (KJN) models. Overall, this work presents a useful tool for understanding and designing mixed-matrix membranes with tubular fillers.
基于膜的工艺被认为是一种有前途的分离方法,可用于许多化学和环境应用,如渗透蒸发和气体分离。由于其良好的传输性能、易于制造以及单位膜面积相对较低的制造成本,许多聚合物膜已被用于这些工艺。然而,这类膜存在渗透性和选择性之间的权衡。混合基质膜,即由嵌入聚合物基质中的填料相组成,已出现以试图部分克服传统聚合物膜和无机膜的一些局限性。其中,包含管状填料的膜是具有超越罗布森上限潜力的新型纳米材料。使纳米管在主体聚合物基质中沿渗透方向排列可显著提高膜的渗透性。然而,尽管已投入大量精力对纳米管混合基质膜进行实验评估,但其建模大多基于复合膜中传质的早期理论。在本研究中,通过数值求解菲克扩散方程计算膜内稳态浓度分布,从而估算含管状填料的混合基质膜的有效渗透率。采用这种方法,评估了各种结构参数的影响,包括管状填料体积分数、取向、长径比和渗透率比。垂直排列的纳米管可提高相对渗透率。相对渗透率随填料 - 聚合物渗透率比、填料体积分数和长径比的增加而增加。对于水 - 丁醇分离,使用聚二甲基硅氧烷与纳米管的混合基质膜在渗透率和选择性方面并未带来性能提升。然后将结果与麦克斯韦、汉密尔顿 - 克罗斯纳和康 - 琼斯 - 奈尔(KJN)模型等分析预测模型进行比较。总体而言,这项工作为理解和设计含管状填料的混合基质膜提供了一个有用的工具。