The
strategy of the tandem hydroformylation reaction for C3 oxygenate
production from CO2 and ethane represents an opportunity
to simultaneously upgrade greenhouse gas CO2 and the large-reserved
shale gas into value-added liquid products. One of the challenges
is how to tune and achieve the appropriate ethylene/CO/H2 ratios for the downstream hydroformylation. Herein, we analyze and
identify the desired ethylene/CO/H2 ratios by considering
different combinations of main and side reactions of CO2 and ethane, based on which the PtSn3/γ-Al2O3 catalyst was identified as promising to enable the
catalytic tandem hydroformylation reaction. The combined studies of
reactor evaluation, in situ and ex situ characterizations, and theoretical calculations revealed that the
Pt cluster/SnO
x
interfacial structures
dominated the simultaneous dehydrogenation and dry reforming of ethane,
thereby allowing the coformation of ethylene, CO, and H2 that were subsequently converted into C3 oxygenates in the tandem
hydroformylation reactor. The current work not only demonstrates the
design principles of suitable catalysts for the tandem-reactor strategy
but also highlights the utilization of CO2 and shale gas
to produce value-added oxygenate products.