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Non-equilibrium molecular dynamics simulation studies on gas permeation across carbon membranes with different pore shape composed of micro-graphite crystallites

机译:非平衡分子动力学模拟研究由微石墨微晶组成的不同孔径的碳膜上的气体渗透

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The molecular simulations have been performed on the permeation of pure and mixed-gases across carbon membranes with three different pore shapes: the diamond path (DP), zigzag path (ZP) and straight path (SP), composed of micro-graphite crystallites. The smallest pore width of the membranes was set at 0.5 nm and the methane and ethane, whose molecular size in the shortest diameter is approximate1y 0.37-0.38 nm, were chosen as permeating gases. The density profiles of methane and ethane showed that the permeation resistance inside the DP and ZP membranes was significant while the resistance of the SP membrane was localized at the membrane exit. In the case of mixed-gas permeation, the permselectivities of ethane to methane were larger than the ideal separation factors for the three membranes due to the competitive adsorption of ethane which was a strongly adsorbed component. However. the permselectivities were smaller than the adsorption equilibrium separation factors since the higher permeation resistance of ethane played a role of counteraction. It is therefore suggested that two factors, selective adsorptions and permeation resistances, should be considered for a rational design of membranes suitable for the separation of specified species in gas mixtures.
机译:对纯气体和混合气体在具有三种不同孔形状的碳膜上的渗透进行了分子模拟:金刚石路径(DP),锯齿形路径(ZP)和直线路径(SP),由微石墨微晶组成。将膜的最小孔宽度设定为0.5nm,并选择甲烷和乙烷作为渗透气体,所述甲烷和乙烷的最短直径的分子大小约为0.37-0.38nm。甲烷和乙烷的密度曲线表明,DP和ZP膜内部的渗透阻力很明显,而SP膜的阻力则局限于膜出口。在混合气体渗透的情况下,由于乙烷的竞争性吸附(强烈吸附的组分),乙烷对甲烷的渗透选择性大于三个膜的理想分离因子。然而。渗透率小于吸附平衡分离因子,因为乙烷的较高的抗渗透性起到了抵消作用。因此建议为合理设计适合分离气体混合物中特定物质的膜,应考虑选择性吸附和抗渗透性这两个因素。

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