Abstract
The separation of complex liquid hydrocarbon mixtures was recently demonstrated using the glassy polymer SBAD-1, showing that small molecule fractionation is possible by such organic membrane materials. Here, we develop a framework that will enable workable predictions of permeate flux and composition in complex hydrocarbon liquids through intrinsically porous glassy polymers. The predictions are made by incorporating experimentally-derived unary sorption and diffusion parameters in a Maxwell-Stefan framework coupled with multicomponent sorption models and various distinct diffusion phenomena. Across the range of sorption and diffusion phenomena considered, both the conventional Flory-Huggins model and the proposed Langmuir + Flory-Huggins sorption model combined with a simple average guest diffusivity or a more complex free-volume theory-based transport resulted in the lowest prediction error for three chosen multicomponent separations. The proposed Maxwell-Stefan framework simply requires pure component transport parameters to allow a fast approximation of the separation of multicomponent liquid hydrocarbon feeds that can potentially be extended to more complex feeds such as crude oil fractions.
Original language | English |
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Article number | 119767 |
Journal | Journal of Membrane Science |
Volume | 640 |
DOIs | |
State | Published - Dec 15 2021 |
Externally published | Yes |
Funding
This work was supported by ExxonMobil Research and Engineering. K.A.T. acknowledges support from the Department of Education Graduate Assistance in Areas of National Need (GAANN) program at Georgia Institute of Technology (award no. P200A180075). This material is also based upon work supported by the U.S. Department of Energy's Office of Energy Efficiency and Renewable Energy ( EERE ) under the Advanced Manufacturing Office (award no. DE-EE0007888). This work was supported by ExxonMobil Research and Engineering. K.A.T. acknowledges support from the Department of Education Graduate Assistance in Areas of National Need (GAANN) program at Georgia Institute of Technology (award no. P200A180075). This material is also based upon work supported by the U.S. Department of Energy's Office of Energy Efficiency and Renewable Energy (EERE) under the Advanced Manufacturing Office (award no. DE-EE0007888).Helium pycnometry was conducted by Micromeritics Analytical Services- The Particle Testing Authority. We thank A.G. Livingston (Imperial College London, Queen Mary University of London) and D. Kim (Imperial College London) for crosslinked PEI support fabrication, B.D. Marshall (ExxonMobil Research and Engineering) for suggesting the free volume theory, M. L. Jue (Georgia Institute of Technology) for the synthesis of PIM-1 and Y. Ma (Georgia Institute of Technology) for the fabrication of dense PIM-1 films. We thank W.J. Koros (Georgia Institute of Technology) for the derivation of the multi-component Flory-Huggins isotherm and for discussions on the sorp-vection concept.
Keywords
- Complex mixtures
- Liquid hydrocarbons
- Maxwell-Stefan
- Organic solvent reverse osmosis
- Polymer membrane