In
this study, a high-pressure membrane reactor (MR) was employed
to carry out the methanol synthesis (MeS) reaction. Syngas was fed
into the MR shell side where a commercial MeS catalyst was used, while
the tube side was swept with a high boiling point liquid with good
solubility toward methanol. A mesoporous alumina ceramic membrane
was utilized after its surface had been modified to be rendered more
hydrophobic. The efficiency of the MR was investigated under a variety
of experimental conditions (different pressures, temperatures, sweep
liquid flow rates, and types of sweep liquids). The results reveal
improved per single-pass carbon conversions when compared to the conventional
packed-bed reactor. An ionic liquid (IL), 1-ethyl-3-methylimidazolium
tetrafluoroborate, was utilized in the MR as the sweep liquid. The
experimental results are compared to those previously reported by
our group (J. Membrane Sci.2019570103) while using a conventional petroleum-derived
solvent as sweep liquid, tetraethylene glycol dimethyl ether (TGDE).
Enhanced carbon conversion (over the petroleum-derived solvent) was
obtained using the IL.