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
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.
Authors
- Jasan Robey Mangalindan (ORCID: https://orcid.org/0009-0004-6102-8995)
- Manish Shetty (ORCID: https://orcid.org/0000-0002-8611-7415)
- Fatima Mahnaz (ORCID: https://orcid.org/0000-0002-7036-8607)
- Jenna Vito
- Navaporn Suphavilai
Institutions
- Texas A&M University (US)
Publication Details
- Journal
- ACS Engineering Au
- Published
- 2025-04-08
- DOI
- https://doi.org/10.1021/acsengineeringau.5c00008
- Citations
- 4
- Primary Topic
- Catalysts for Methane Reforming
- Type
- article
- Field-Weighted Citation Impact
- 1.56
Funders
- Artie McFerrin Department of Chemical Engineering, Texas A and M University
- Texas A and M Engineering Experiment Station, Texas A and M University
- College of Engineering, Texas A and M University
- Division of Chemical, Bioengineering, Environmental, and Transport Systems