Influence of Single-Layer Porous Graphene Membrane Structure on C2 Hydrocarbons Separation Performance: A Molecular Dynamics Study
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Graphical Abstract
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Abstract
C2 hydrocarbons are important intermediates in petrochemical industry. Cryogenic rectification is broadly used to separate mixed C2 hydrocarbon gas to obtain pure C2 products. However, this process is very energy-consuming. Employing membrane separation technology to separate mixed gases can effectively reduce costs and energy consumption. Single-layer porous graphene membranes have great potential for mixed C2 hydrocarbons gas separation because of their outstanding separation performance; however, relevant studies are scarce. Herein, molecular dynamics simulations are applied to study the effect on the efficiency and selectivity of C2 hydrocarbons gas separation by single-layer porous graphene membranes with different pore sizes, pore shapes, and modified functional groups. The results show that the single-layer porous graphene membranes with pore sizes of 0.444—0.484 nm facilitate ethane retention with high ethylene passability. High gas passability and selectivity are determined for circular and oval pores, respectively. Oval pores with a short diameter of 0.510 nm and a long diameter of 1.164 nm are able to effectively pass ethylene molecules while retaining ethane molecules. A pore size of 0.596 nm with the pore being modified with two carboxyl groups can retain ethylene and pass acetylene. Our simulation results provide theoretical insights into the design of single-layer porous graphene membranes to separate C2 hydrocarbons gases efficiently and selectively.
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