TY - JOUR
T1 - Molecular Design of Precise Network Polymerized Ionic Liquid Membranes for Toluene/Heptane Separations
AU - Sheridan, Grant S.
AU - Evans, Christopher M.
N1 - Publisher Copyright:
© 2019 American Chemical Society.
PY - 2019/8/7
Y1 - 2019/8/7
N2 - Precise network polymerized ionic liquid membranes with tethered imidazolium cations, variable anion, and controlled cross-link density were developed to understand how molecular structure impacts solubility and diffusion in the context of toluene/heptane separations. Switching the anion from tetrafluoroborate (BF4) to bis(trifluoromethane sulfonimide) led to a 25 K drop in the glass transition temperature, concomitant increase in penetrant diffusion coefficients, and increased solubility of toluene relative to heptane. Reducing cross-link density led to an increase in toluene swelling, while heptane uptake remained relatively low and constant. Interestingly, differences in toluene and heptane diffusion coefficients exhibited a maximum at intermediate cross-link density. It is hypothesized that a fully cross-linked network has a mesh size small enough to impede transport, while lower cross-link densities allow toluene to swell the system to a greater extent, in contrast to heptane. The interplay of diffusion and solubility effects lead to a nonmonotonic trend in selectivity, which will inform the design of membranes as effective organic liquid separations media.
AB - Precise network polymerized ionic liquid membranes with tethered imidazolium cations, variable anion, and controlled cross-link density were developed to understand how molecular structure impacts solubility and diffusion in the context of toluene/heptane separations. Switching the anion from tetrafluoroborate (BF4) to bis(trifluoromethane sulfonimide) led to a 25 K drop in the glass transition temperature, concomitant increase in penetrant diffusion coefficients, and increased solubility of toluene relative to heptane. Reducing cross-link density led to an increase in toluene swelling, while heptane uptake remained relatively low and constant. Interestingly, differences in toluene and heptane diffusion coefficients exhibited a maximum at intermediate cross-link density. It is hypothesized that a fully cross-linked network has a mesh size small enough to impede transport, while lower cross-link densities allow toluene to swell the system to a greater extent, in contrast to heptane. The interplay of diffusion and solubility effects lead to a nonmonotonic trend in selectivity, which will inform the design of membranes as effective organic liquid separations media.
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U2 - 10.1021/acs.iecr.9b03059
DO - 10.1021/acs.iecr.9b03059
M3 - Article
AN - SCOPUS:85071319307
SN - 0888-5885
VL - 58
SP - 14389
EP - 14395
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 31
ER -