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.

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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
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article
Field-Weighted Citation Impact
1.56

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article

Tandem Cu/ZnO/ZrO 2 -SAPO-34 System for Dimethyl Ether Synthesis from CO 2 and H 2 : Catalyst Optimization, Techno-Economic, and Carbon-Footprint Analyses

Jasan Robey Mangalindan, Manish Shetty, Fatima Mahnaz, Jenna Vito et al.
4 citations
ACS Engineering Au
Catalysts for Methane Reforming
1.56
article

Tandem Cu/ZnO/ZrO 2 -SAPO-34 System for Dimethyl Ether Synthesis from CO 2 and H 2 : Catalyst Optimization, Techno-Economic, and Carbon-Footprint Analyses

Jasan Robey Mangalindan, Manish Shetty, Fatima Mahnaz, Jenna Vito, Navaporn Suphavilai
article en
4 citations

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.

ACS Engineering AuVol. 5(3)
Texas A&M University (US)
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
Openalex Percentile: Top 18%
Catalysts for Methane Reforming
1.56
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