In the vast majority of studies, methanol production
via CO2 hydrogenation is realized using bifunctional catalysts,
commonly
CuZnO phases. The basic motivation of this study is to confront main
concerns regarding typical copper-based catalysts, which are the aggregation
of the active metal nanoparticles (NPs) and its concomitant deactivation.
For this, an extensive research on composites of mesoporous iron trimesate
metal–organic frameworks (MOFs) [crystalline MIL-100(Fe) and
semiamorphous FeBTC], loaded with copper clusters (CuCs) into the
pores, is performed, because it is a pioneer in the area. The growth
and aggregation of CuCs are hindered by the confinement of the active
entities into the MOF mesocages. From the two studied MOFs, only the
copper loaded semiamorphous FeBTC behaves as a catalyst. To further
enhance the catalytic activity, CuCs@FeBTC NPs are dispersed on the
plates constituting a reduced graphene-oxide aerogel. Main steps in
the preparation of these complex catalysts involve the use of sustainable
technology based on supercritical CO2, used either as a
solvent or drying agent. The reduction strategy designed to obtain
the active catalyst (Cu2+ to Cu+/Cu0 in CuCs) was crucial to upgrade the end product performance. A double
reduction route, applying ascorbic acid preceding thermal H2 reduction, turns out to be necessary to attain a significant catalytic
activity of the confined Cu2+ species. The as-synthesized
and spent catalysts were analyzed in regard of the structure (X-ray
diffraction, infrared), bulk (mass spectrometry) and surface (X-ray
photoelectron spectroscopy) composition, morphology (microscopy and
energy dispersive spectroscopy) and textural properties (N2 physisorption). The catalytic performance of reduced CuCs@FeBTC
and [CuCs@FeBTC]@rGO composites was tested in the CO2 hydrogenation
reaction at 10 bar. Methane and methanol were obtained as valuable
reaction products. When using the [CuCs@FeBTC]@rGO aerogel, methanol
yield was noticeably high, in comparison to reported data, in the
order of 86 mgMeOHgCu
–1 h–1; while the amount of side products (methane, CO)
was almost totally hindered up to 260 °C.