Premium
Effects of molecular simulation parameters on predicting gas separation performance of ZIFs
Author(s) -
Ozcan Aydin,
Keskin Seda
Publication year - 2015
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.4482
Subject(s) - selectivity , adsorption , membrane , gas separation , nanoporous , permeation , chemistry , sorbent , chemical engineering , selective adsorption , molecular dynamics , force field (fiction) , permeability (electromagnetism) , membrane technology , chromatography , materials science , organic chemistry , computational chemistry , catalysis , computer science , engineering , biochemistry , artificial intelligence
BACKGROUND A significant number of molecular simulation studies exist in the literature for assessing single‐component gas adsorption capacities of ZIFs and all these simulations were performed using different force field parameters. In this study, molecular simulations were carried out to predict both adsorption‐based and membrane‐based separation performances of ZIF ‐68 and ZIF ‐69 for CH 4 / H 2 , CH 4 / N 2 , CO 2 / CH 4 , CO 2 / H 2 and CO 2 / N 2 mixtures using three different force fields. RESULTS Results showed that adsorption selectivity of ZIFs may vary significantly depending on the force field parameters whereas membrane selectivity is much less sensitive to the force field. In addition to adsorption and membrane selectivities, various separation properties of ZIFs were estimated such as working capacity, sorbent selection parameter, regenerability, permeability and compared with the properties of other well‐known nanoporous adsorbents and membranes. CONCLUSION Comparison of separation performance of ZIF ‐68 and ZIF ‐69 with traditional zeolites showed that ZIFs can be promising adsorbent materials for CH 4 / H 2 , CH 4 / N 2 , CO 2 / CH 4 , CO 2 / H 2 separations and promising membrane materials for CH 4 / H 2 and CO 2 / H 2 separations. It is better to use ZIFs as adsorbents rather than membranes since they offer higher adsorption selectivity than permeation selectivity for the gas mixtures we studied. © 2014 Society of Chemical Industry