In this work, we investigate experimentally the use of
zeolite
13X as an efficient water sorbent in the sorption-enhanced CO2 hydrogenation reaction over Cu/ZnO/Al2O3 under different operating conditions and over multiple reaction–regeneration
cycles. Introduction of the solid sorbent along with the catalyst
in the reactor leads to a prominent increase in the CO2 conversion and CH3OH yield. As the reaction proceeds,
the sorbent gradually becomes saturated, the enhancement effect reduces,
and the system eventually reaches the same steady state as with catalyst
only. The CH3OH yield increase is higher than that of the
CO2 conversion, indicating preferential enhancement of
methanol production. This can be attributed to the partial co-adsorption
of both methanol and water on zeolite 13X. The effects of reaction
and regeneration temperature on the activity, product distribution,
enhancement degree, and recyclability are also examined. The highest
sorption enhancement occurs at 225 °C, with the methanol yield
increasing by 115% compared to the conventional process. The cyclic
stability is investigated by consecutive reaction–regeneration
cycles. The correlation between activity reduction and textural properties
of both the catalyst and sorbent as well as the zeolite’s ability
to regenerate are explored. To that end, the effect of regeneration
temperature on the products’ desorption is also examined.