School of Chemical Engineering , The University of Queensland , Brisbane , QLD 4072 , Australia.
ACS Appl Mater Interfaces. 2018 Oct 10;10(40):34706-34717. doi: 10.1021/acsami.8b08886. Epub 2018 Sep 25.
We have used nonequilibrium molecular dynamics simulations to investigate the transport diffusion of methane, at 300 K and pressures of up to 15 bar, in 30 nm-long (10, 10) carbon nanotubes (CNTs) held between two flanges mounted at the ends to represent the surface layers of an embedding matrix material. Strong interfacial resistance to the entry and exit of molecules is found in the 30 nm-long CNTs, which reduces their permeability by more than 2 orders of magnitude. Increasing the adsorption affinity and surface area of the flange reduces the interfacial resistance and consequently enhances the methane diffusivity in CNT membranes. Curved streamlines near the flange surface make a significant contribution to the permeability, even when the adsorption on the matrix surface is negligible. We propose a model to calculate the separate components of the interfacial resistance, the flange resistance, which increases with increase in the membrane porosity, and the entrance-exit resistance, which is independent of the membrane porosity. While the flange resistance accounts for the reduction of interfacial resistance with decrease in the membrane porosity, the entrance-exit resistance is responsible for the reduction of interfacial resistance with increase in the flange adsorption affinity. The flange resistivity demonstrates a complex dependency on the flange adsorption affinity, which is attributed to the competition between the enhanced adsorption and the enhanced migration time of the molecules on the flange. It is concluded that the embedding matrix adsorption affinity and membrane porosity separately play critical roles in determining the interfacial resistance and permeability in CNT membranes. Our simulation results can help reduce the interfacial resistance and improve the permeance in CNT membranes by appropriate choice of intertube spacing and flange material and are readily applied to all nanoporous membranes with a passive matrix.
我们使用非平衡分子动力学模拟来研究甲烷在 300 K 和高达 15 巴压力下的传输扩散,在 30nm 长的(10,10)碳纳米管(CNT)中进行,该 CNT 夹在两个安装在两端的法兰之间,以代表嵌入基质材料的表面层。在 30nm 长的 CNT 中发现了对分子进入和退出的强界面阻力,这将其渗透率降低了两个数量级以上。增加法兰的吸附亲和力和表面积会降低界面阻力,从而提高 CNT 膜中的甲烷扩散率。在法兰表面附近的弯曲流线对渗透率有很大的贡献,即使在基质表面上的吸附可以忽略不计。我们提出了一个模型来计算界面阻力的单独组件,即随膜孔隙率增加而增加的法兰阻力,以及与膜孔隙率无关的进出口阻力。虽然法兰阻力解释了界面阻力随膜孔隙率降低而降低,但进出口阻力是界面阻力随法兰吸附亲和力增加而降低的原因。法兰电阻率对法兰吸附亲和力表现出复杂的依赖性,这归因于增强的吸附和分子在法兰上的增强迁移时间之间的竞争。结论是,嵌入基质的吸附亲和力和膜孔隙率分别在确定 CNT 膜中的界面阻力和渗透率方面起着关键作用。我们的模拟结果可以通过选择合适的管间间距和法兰材料来帮助降低界面阻力并提高 CNT 膜的渗透率,并且可以很容易地应用于所有具有被动基质的纳米多孔膜。