Ozcan Aydin, Perego Claudio, Salvalaglio Matteo, Parrinello Michele, Yazaydin Ozgur
Department of Chemical Engineering , University College London , London , WC1E 7JE , UK . Email:
Department of Chemistry and Applied Biosciences , ETH Zurich , Zurich , Switzerland.
Chem Sci. 2017 May 1;8(5):3858-3865. doi: 10.1039/c6sc04978h. Epub 2017 Mar 20.
In this study, we introduce a new non-equilibrium molecular dynamics simulation method to perform simulations of concentration driven membrane permeation processes. The methodology is based on the application of a non-conservative bias force controlling the concentration of species at the inlet and outlet of a membrane. We demonstrate our method for pure methane, ethane and ethylene permeation and for ethane/ethylene separation through a flexible ZIF-8 membrane. Results show that a stationary concentration gradient is maintained across the membrane, realistically simulating an out-of-equilibrium diffusive process, and the computed permeabilities and selectivity are in good agreement with experimental results.
在本研究中,我们引入了一种新的非平衡分子动力学模拟方法,以进行浓度驱动的膜渗透过程模拟。该方法基于应用非保守偏置力来控制膜入口和出口处物质的浓度。我们展示了该方法用于纯甲烷、乙烷和乙烯的渗透以及通过柔性ZIF-8膜进行乙烷/乙烯分离的情况。结果表明,膜两侧维持着稳定的浓度梯度,逼真地模拟了非平衡扩散过程,并且计算得到的渗透率和选择性与实验结果吻合良好。