To alleviate detrimental effects associated with anthropogenic
emissions, the use of CO2 and H2 as feedstocks
for their conversion to dimethyl ether (DME) with tandem catalysts
is an attractive and sustainable route. First, we investigated the
catalytic activity of bifunctional admixtures of Cu-ZnO-ZrO2 (CZZ) and a silicoaluminophosphate, SAPO-34, for CO2 hydrogenation
to DME and optimized their reactivity with an emphasis on identifying
optimum synthesis conditions for CZZ including Cu:Zn:Zr molar ratio
and aging and calcination temperatures. The highest methanol (MeOH)
productivity (10.8 mol kgcat–1 h–1) was observed for CZZ-611 aged at 40 °C and
calcined at 500 °C. When coupled with SAPO-34, CZZ/SAPO-34 reached
20% CO2 conversion and 56% DME selectivity at optimized
conditions (260 °C, 500 psig, and 2000 mL gCZZ–1 h–1) and was stable for 50 h time-on-stream,
with a slight reduction in activity. Next, we performed kinetic modeling
to translate lab-scale findings to industrial packed-bed reactors
followed by a techno-economic analysis (TEA) with cradle-to-gate environmental
footprint evaluation to evaluate its industrial applicability. A TEA
of a 20,000 tpy DME plant revealed raw material costs as the main
operating cost drivers (H2 cost comprises 47% of total
cost). Considering green H2 ($4/kg H2) and captured
CO2 as feed, the minimum DME selling price (MDSP) was $3.21/kg,
∼2.7× higher than the market price ($1.2/kg). MDSP drops
to $1.99/kg with gray H2 ($1/kg H2) and fluctuates
±$0.14 with changes in CAPEX (±30%) and other economic factors.
The plant’s carbon footprint was mainly affected by the H2 source. Green and gray H2 resulted in emissions
of 0.21 and 4.4 kg CO2 eq/kg DME, respectively. Importantly,
a negative carbon footprint can be achieved by using green H2 and CO2 captured directly from air. Overall, our work
shows tandem catalysis as a promising approach toward sustainable
DME production and identifies the pathway toward making it cost-competitive
with fossil fuels.