The performance of a dense ceramic
hydrogen-permeable membrane
reactor for the nonoxidative methane dehydroaromatization (MDA), according
to the equilibrium reaction 6CH4 ⇆ C6H6 + 9H2 with a 6 wt % Mo/HZSM-5 bifunctional
catalyst was investigated. A U-shaped ceramic hollow fiber membrane
of the composition La5.5W0.6Mo0.4O11.25−δ (LWM0.4) has been used
for the in situ removal of H2 to overcome
thermodynamic constraints. The yield of aromatics (benzene, toluene,
naphthalene) in the MDA could be increased in the beginning of the
aromatization reaction by ∼50%–70%, in comparison with
the fixed-bed reactor, because 40%–60% of the H2 abstracted have been extracted at 700 °C with a weight hourly
space velocity (WHSV) of 840 cm3 gcat
–1 h–1. These advantages of the membrane reactor
operation decrease with time on stream, since the removal of H2 boosts not only CH4 conversion and yield of aromatics,
but also catalyst deactivation by deposition of carbonaceous deposits.
However, the catalyst system could be regenerated by burning the coke
away with air.