Peer-reviewed veterinary case report
Tandem Cu/ZnO/ZrO<sub>2</sub>‑SAPO-34 System for Dimethyl Ether Synthesis from CO<sub>2</sub> and H<sub>2</sub>: Catalyst Optimization, Techno-Economic, and Carbon-Footprint Analyses.
- Year:
- 2025
- Authors:
- Mangalindan JR et al.
- Affiliation:
- Artie McFerrin Department of Chemical Engineering · United States
- Species:
- cat
Abstract
To alleviate detrimental effects associated with anthropogenic emissions, the use of CO<sub>2</sub> and H<sub>2</sub> 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-ZrO<sub>2</sub> (CZZ) and a silicoaluminophosphate, SAPO-34, for CO<sub>2</sub> 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 kg<sub>cat</sub> <sup>-1</sup> h<sup>-1</sup>) was observed for CZZ-611 aged at 40 °C and calcined at 500 °C. When coupled with SAPO-34, CZZ/SAPO-34 reached 20% CO<sub>2</sub> conversion and 56% DME selectivity at optimized conditions (260 °C, 500 psig, and 2000 mL g<sub>CZZ</sub> <sup>-1</sup> h<sup>-1</sup>) 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 (H<sub>2</sub> cost comprises 47% of total cost). Considering green H<sub>2</sub> ($4/kg H<sub>2</sub>) and captured CO<sub>2</sub> 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 H<sub>2</sub> ($1/kg H<sub>2</sub>) and fluctuates ±$0.14 with changes in CAPEX (±30%) and other economic factors. The plant's carbon footprint was mainly affected by the H<sub>2</sub> source. Green and gray H<sub>2</sub> resulted in emissions of 0.21 and 4.4 kg CO<sub>2</sub> eq/kg DME, respectively. Importantly, a negative carbon footprint can be achieved by using green H<sub>2</sub> and CO<sub>2</sub> 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.
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Search related cases →Original publication: https://europepmc.org/article/MED/40556642