A selective
and stable alumina-supported In-promoted Fe catalyst
(10 mol % In based on Fe) was discovered for converting syngas (2:1
H2/CO ratio) to olefins with high selectivity (45% with
CO2 included) and a remarkable stability (72 h run) at
a CO conversion of 10% at 400 °C and 5 bar. The X-ray photoelectron
spectroscopy results indicated that incorporating In into Fe catalysts
changed the chemical bonding state of Fe and Fe/In composition near
the surface layers, which affected the catalytic reactivity. Steady-state
isotopic transient kinetic analysis showed that more stable CHx fragments
are present on the catalyst surface when incorporating In into Fe,
which can promote C–C coupling reaction toward olefins. Our
study demonstrates that introducing In into Fe catalysts on Al2O3 support can lower CO activation abilities. It
has more impacts on lowering hydrogenation activity, which permits
more C–C couplings and like of “ene” hydrogenation.
Moreover, weakening CO adsorption both in terms of sites and strength
encouraged CO toward hydrocarbons rather than CO2.