TY - JOUR
T1 - Assessing the viability of K-Mo2C for reverse water-gas shift scale-up
T2 - Molecular to laboratory to pilot scale
AU - Juneau, Mitchell
AU - Vonglis, Madeline
AU - Hartvigsen, Joseph
AU - Frost, Lyman
AU - Bayerl, Dylan
AU - Dixit, Mudit
AU - Mpourmpakis, Giannis
AU - Morse, James R.
AU - Baldwin, Jeffrey W.
AU - Willauer, Heather D.
AU - Porosoff, Marc D.
N1 - Publisher Copyright:
© 2020 The Royal Society of Chemistry.
PY - 2020/8
Y1 - 2020/8
N2 - Conversion of CO2 to value-added chemicals and fuels is a potentially valuable route for renewable energy storage and a future CO2-neutral economy. The first step is CO2 conversion to CO via the reverse water-gas shift (RWGS) reaction. Effluent CO can then be hydrogenated to chemicals and fuels via Fischer-Tropsch (FT) synthesis over a tandem catalyst or within a second reactor. To implement this process on an industrial scale, low-cost, scalable and highly-selective catalysts are required, prompting investigations into materials that meet these design constraints. Potassium-promoted molybdenum carbide supported on gamma alumina (K-Mo2C/?-Al2O3) has recently been shown to be a highly active and selective RWGS catalyst in the laboratory, prompting us to investigate the viability of K-Mo2C/?-Al2O3 for scale-up. In this report, laboratory-scale (~100 mg catalyst) reactor studies are extended to the pilot-scale (~1 kg catalyst), and viability for scale-up is tested further with density functional theory (DFT) calculations, detailed characterization and reactor experiments under a range of temperatures (300-600 °C) and flow conditions. The pilot-scale experiments illustrate K-Mo2C/?-Al2O3 is a highly active and selective catalyst (44% CO2 conversion, 98%+ CO selectivity at GHSV = 1.7 L kg-1 s-1 and T = 450 °C) that exhibits no signs of deactivation for over 10 days on stream. Together, experiments across the molecular, laboratory and pilot scales demonstrate that K-Mo2C/?-Al2O3 is an economically-viable RWGS catalyst with promising future applications in the US Naval Research Laboratory's seawater-to-fuel process, downstream methanol synthesis and FT.
AB - Conversion of CO2 to value-added chemicals and fuels is a potentially valuable route for renewable energy storage and a future CO2-neutral economy. The first step is CO2 conversion to CO via the reverse water-gas shift (RWGS) reaction. Effluent CO can then be hydrogenated to chemicals and fuels via Fischer-Tropsch (FT) synthesis over a tandem catalyst or within a second reactor. To implement this process on an industrial scale, low-cost, scalable and highly-selective catalysts are required, prompting investigations into materials that meet these design constraints. Potassium-promoted molybdenum carbide supported on gamma alumina (K-Mo2C/?-Al2O3) has recently been shown to be a highly active and selective RWGS catalyst in the laboratory, prompting us to investigate the viability of K-Mo2C/?-Al2O3 for scale-up. In this report, laboratory-scale (~100 mg catalyst) reactor studies are extended to the pilot-scale (~1 kg catalyst), and viability for scale-up is tested further with density functional theory (DFT) calculations, detailed characterization and reactor experiments under a range of temperatures (300-600 °C) and flow conditions. The pilot-scale experiments illustrate K-Mo2C/?-Al2O3 is a highly active and selective catalyst (44% CO2 conversion, 98%+ CO selectivity at GHSV = 1.7 L kg-1 s-1 and T = 450 °C) that exhibits no signs of deactivation for over 10 days on stream. Together, experiments across the molecular, laboratory and pilot scales demonstrate that K-Mo2C/?-Al2O3 is an economically-viable RWGS catalyst with promising future applications in the US Naval Research Laboratory's seawater-to-fuel process, downstream methanol synthesis and FT.
UR - http://www.scopus.com/inward/record.url?scp=85089900218&partnerID=8YFLogxK
U2 - 10.1039/d0ee01457e
DO - 10.1039/d0ee01457e
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AN - SCOPUS:85089900218
SN - 1754-5692
VL - 13
SP - 2524
EP - 2539
JO - Energy and Environmental Science
JF - Energy and Environmental Science
IS - 8
ER -