Fischer–Tropsch
has become an indispensable choice in the
gas-to-liquid conversion reactions to produce a wide range of petrochemicals
using recently emerging biomass or other types of feedstock such as
coal or natural gas. Herein we report the incorporation of novel Cu
nanoparticles with two Fischer–Tropsch synthesis (FTS) catalytic
systems, Fe/reduced graphene oxide (rGO) and Fe–Mn/rGO, to
evaluate their FTS performance and olefin productivity in two types
of reactors: slurry-bed reactor (SBR) and fixed-bed reactor (FBR).
Four catalysts were compared and investigated, namely Fe, FeCu7, FeMn10Cu7, and FeMn16,
which were highly dispersed over reduced graphene oxide nanosheets.
The catalysts were first characterized by transmission electron microscopy
(TEM), nitrogen physisorption, X-ray fluorescence (XRF), X-ray diffraction
(XRD), and H-TPR techniques. In the SBR, Cu enhanced olefinity only
when used alone in FeCu7 without Mn promotion. When used
with Mn, the olefin yield was not changed, but light olefins decreased
slightly at the expense of heavier olefins. In the FBR system, Cu
as a reduction promoter improved the catalyst activity. It increased
the olefin yield mainly due to increased activity, even if the CO2 decreased by the action of Cu promoters. The olefinity of
the product was improved by Cu promotion but it did not exceed the
landmark made by FeMn16 at 320 °C. The paraffinity
was also enhanced by Cu promotion especially in the presence of Mn,
indicating a strong synergistic effect. Cu was found to be better
than Mn in enhancing the paraffin yield, while Mn is a better olefin
yield enhancer. Finally, Cu promotion was found to enhance the selectivity
towards light olefins C2–4. This study gives a deep insight
into the effect of different highly dispersed FTS catalyst systems
on the olefin hydrocarbon productivity and selectivity in two major
types of FTS reactors.