Ethylene/ethane separation via cryogenic distillation is extremely energy‐intensive, and membrane separation may provide an attractive alternative. In this paper, ethylene/ethane separation performance using polymeric membranes is summarized, and an experimental ethylene/ethane polymeric upper bound based on literature data is presented. A theoretical prediction of the ethylene/ethane upper bound is also presented, and shows good agreement with the experimental upper bound. Further, two ways to overcome the ethylene/ethane upper bound, based on increasing the sorption or diffusion selectivity, is also discussed, and a review on advanced membrane types such as facilitated transport membranes, zeolite and metal organic framework based membranes, and carbon molecular sieve membranes is presented. Of these, carbon membranes have shown the potential to surpass the polymeric ethylene/ethane upper bound performance. Furthermore, a convenient, potentially scalable method for tailoring the performance of carbon membranes for ethylene/ethane separation based on tuning the pyrolysis conditions has also been demonstrated. © 2013 American Institute of Chemical Engineers AIChE J, 59: 3475–3489, 2013

Characterization techniques beyond microscopy, scattering and spectroscopy approaches are needed to understand and improve sub-angstrom discrimination between penetrants in carbon molecular sieve (CMS) membranes. Here we use a method based on molecular scale gas diffusion probes to understand relevant membrane properties at the required level of detail. We further use this method to consider hypotheses about the evolution of structure responsible for fundamental properties of CMS materials derived from a high performance CMS precursor polymer, 6FDA:BPDA-DAM. While 6FDA:BPDA-DAM derived CMS membranes display a ~230 % improvement in CO 2 permeability when compared to Matrimid ® derived CMS formed under the same conditions, the diffusional selectivity for these two materials are very similar at 35 and 38.5, respectively. These results indicate a non-trivial connection between CMS precursor material structure and resulting performance. Linking hypotheses about structural changes likely to occur during pyrolysis with the probe data provides insights regarding transformation of the random coil polyimide into ultra-rigid CMS, with exquisite size and shape diffusion selectivity. The results provide a framework for understanding and tuning properties of this special class of materials with important technological advantages in energy-intensive gas separations.

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We report the computational discovery and experimental evaluation of nanoporous materials targeted at the adsorptive separation of p-xylene from a C 8 aromatics mixture. We first introduce a computational method that is capable of efficiently predicting the p-xylene selectivities and capacities for a large database of porous materials. We then demonstrate the application of this method to screen a database of several thousand metal−organic framework (MOF) structures. Our computational screening methodology predicted that two MOFs with good solvothermal stability and commercially available linkers give comparable performance to the state-of-the-art zeolite BaX currently used in industrial p-xylene separations. The bestperforming MOFs are then synthesized, and their xylene separation characteristics are evaluated in detail through breakthrough adsorption experiments and modeling. We find that the selectivities obtained in these materials are higher than that of any MOF previously reported in the literature and in some cases exceed the measured performance of zeolite BaX. In the case of the pxylene selective material MOF-48, we use calculated free energy profiles to show how the presence of methyl substituents on the linkers allows the inversion of selectivity from the equivalent MOF with no methyl substituents (MIL-47, which is o-xylene selective). This combined computational and experimental methodology is a useful step in the development of MOFs for separation of aromatic hydrocarbons and can also be applied to other chemical separations and other classes of porous materials as long as the appropriate intermolecular force fields are available.

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